WorldWideScience

Sample records for pulverized coal boilers

  1. NOx control in large-scale power plant boilers through superfine pulverized coal technology

    Institute of Scientific and Technical Information of China (English)

    Jie YIN; Jianxing REN; Dunsong WEI

    2008-01-01

    Superfine pulverized coal technology can effectively reduce NOx emission in coal-fired power plant boilers. It can also economize the cost of the power plant and improve the use of the ash in the flue gas. Superfine pulverized coal technology, which will be widely used in China, includes common superfine pulverized coal technology and superfine pulverized coal reburning technology. The use of superfine pulver-ized coal instead of common coal in large-scale power plants will not only reduce more than 30% of NOx emission but also improve the thermal efficiency of the boiler.

  2. Pulverized-coal-firing small-size boiler for coal-cartridge system

    Energy Technology Data Exchange (ETDEWEB)

    1986-12-01

    Kawasaki Heavy Industries, Ltd. supplied a test boiler plant to the Iwakuni Experimental Station of the Coal Cartridge System (CCS) Promotion Association in September 1985; this was the first pulverized-coal-fired small industrial boiler in Japan. Tests will be performed for two years, until fiscal 1987, at the CCS Iwakuni Experimental Station to establish a method of coal-firing with a performance comparable to heavy oil firing. The boiler plant has been operating satisfactorily.

  3. Study on the NOx release rule along the boiler during pulverized coal combustion

    Institute of Scientific and Technical Information of China (English)

    JIN Jing; ZHANG Zhongxiao; LI Ruiyang

    2007-01-01

    Numerical simulation and experimental study on NOx release along the boiler during pulverized coal combustion have been conducted.With the increase of temperature the NOx emission increased and the peak value of NOx release moved forward.But when the temperature increased to a certain degree,NOx emission began to reduce.NOx emission increased with the increase of nitrogen content of coal.The peak value of NOx release moved backwards with the increase of coal rank.NOx emission increased obviously with the increase of stoichiometric ratio.There existed a critical average diameter of the pulverized coal (de).If d≤dc,NOx emission reduced with the decrease of pulverized coal size.If d>de,NOx emission reduced with the increase of the pulverized coal size.The results showed that the simulation results are in agreement with the experimental results for concentration distribution of NOx along the axis of the furnace.

  4. Advanced char burnout models for the simulation of pulverized coal fired boilers

    Energy Technology Data Exchange (ETDEWEB)

    T. Severin; S. Wirtz; V. Scherer [Ruhr-University, Bochum (Germany). Institute of Energy Plant Technology (LEAT)

    2005-07-01

    The numerical simulation of coal combustion processes is widely used as an efficient means to predict burner or system behaviour. In this paper an approach to improve CFD simulations of pulverized coal fired boilers with advanced coal combustion models is presented. In simple coal combustion models, first order Arrhenius rate equations are used for devolatilization and char burnout. The accuracy of such simple models is sufficient for the basic aspects of heat release. The prediction of carbon-in-ash is one aspect of special interest in the simulation of pulverized coal fired boilers. To determine the carbon-in-ash levels in the fly ash of coal fired furnaces, the char burnout model has to be more detailed. It was tested, in how far changing operating conditions affect the carbon-in-ash prediction of the simulation. To run several test cases in a short time, a simplified cellnet model was applied. To use a cellnet model for simulations of pulverized coal fired boilers, it was coupled with a Lagrangian particle model, used in CFD simulations, too. 18 refs., 5 figs., 5 tabs.

  5. Modeling and optimization of processes for clean and efficient pulverized coal combustion in utility boilers

    Directory of Open Access Journals (Sweden)

    Belošević Srđan V.

    2016-01-01

    Full Text Available Pulverized coal-fired power plants should provide higher efficiency of energy conversion, flexibility in terms of boiler loads and fuel characteristics and emission reduction of pollutants like nitrogen oxides. Modification of combustion process is a cost-effective technology for NOx control. For optimization of complex processes, such as turbulent reactive flow in coal-fired furnaces, mathematical modeling is regularly used. The NOx emission reduction by combustion modifications in the 350 MWe Kostolac B boiler furnace, tangentially fired by pulverized Serbian lignite, is investigated in the paper. Numerical experiments were done by an in-house developed three-dimensional differential comprehensive combustion code, with fuel- and thermal-NO formation/destruction reactions model. The code was developed to be easily used by engineering staff for process analysis in boiler units. A broad range of operating conditions was examined, such as fuel and preheated air distribution over the burners and tiers, operation mode of the burners, grinding fineness and quality of coal, boiler loads, cold air ingress, recirculation of flue gases, water-walls ash deposition and combined effect of different parameters. The predictions show that the NOx emission reduction of up to 30% can be achieved by a proper combustion organization in the case-study furnace, with the flame position control. Impact of combustion modifications on the boiler operation was evaluated by the boiler thermal calculations suggesting that the facility was to be controlled within narrow limits of operation parameters. Such a complex approach to pollutants control enables evaluating alternative solutions to achieve efficient and low emission operation of utility boiler units. [Projekat Ministarstva nauke Republike Srbije, br. TR-33018: Increase in energy and ecology efficiency of processes in pulverized coal-fired furnace and optimization of utility steam boiler air preheater by using in

  6. Influence of constricted air distribution on NOx emissions in pulverized coal combustion boiler

    Institute of Scientific and Technical Information of China (English)

    WEI Feng(魏风); ZHANG Jun-ying(张军营); TANG Bi-guang(唐必光); ZHENG Chu-guang(郑楚光)

    2003-01-01

    This paper reports a field testing of full scale PCC (Pulverized Coal Combustion) boiler study into the influence of constricted air distribution on NOx emissions at unit 3 (125 MW power units, 420 t/h boiler) of Guixi power station, Jiangxi and puts forward the methods to decrease NOx emissions and the principle of boiler operation and regulation through analyzing NOx emissions state under real running condition. Based on boiler constricted air distribution, the experiment mainly tested the influence of primary air, excessive air, boiler load and milling sets (tertiary air) on NOx emissions and found its influence characteristics. A degraded bituminous coal is simply adopted to avoid the test results from other factors.

  7. A Pulverized Coal-Fired Boiler Optimized for Oxyfuel Combustion Technology

    Directory of Open Access Journals (Sweden)

    Tomáš Dlouhý

    2012-01-01

    Full Text Available This paper presents the results of a study on modifying a pulverized coal-fired steam boiler in a 250 MWe power plant for oxygen combustion conditions. The entry point of the study is a boiler that was designed for standard air combustion. It has been proven that simply substituting air by oxygen as an oxidizer is not sufficient for maintaining a satisfactory operating mode, not even with flue gas recycling. Boiler design optimization aggregating modifications to the boiler’s dimensions, heating surfaces and recycled flue gas flow rate, and specification of a flue gas recycling extraction point is therefore necessary in order to achieve suitable conditions for oxygen combustion. Attention is given to reducing boiler leakage, to which external pre-combustion coal drying makes a major contribution. The optimization is carried out with regard to an overall power plant conception for which a decrease in efficiency due to CO2 separation is formulated.

  8. Economic Analysis for Rebuilding of an Aged Pulverized Coal-Fired Boiler with a New Boiler in an Aged Thermal Power Plant

    Directory of Open Access Journals (Sweden)

    Burhanettin Cetin

    2013-01-01

    Full Text Available Fossil-fired thermal power plants (TPP produce a significant part of electricity in the world. Because of the aging TPPs and so their equipment (especially boiler, thermal power plants also produce less power than their installed capacities, and there has been power loss in time. This situation affects the supply and demand balance of countries. For this reason, aging equipments such as pulverized coal-fired boiler (PCB must be renewed and power loss must be recovered, instead of building new TPPs. In this study, economic analysis of rebuilding an aged pulverized coal-fired boiler with a new pulverized coal-fired boiler including flue gas desulfurization (FGD unit and a circulating fluidized bed boiler (FBB are investigated in an existing old TPP. Emission costs are also added to model, and the developed model is applied to a 200 MWe pulverized coal-fired thermal power plant in Turkey. As a result, the payback period and the net present value are calculated for different technical and economic parameters such as power loss, load factor, electricity price, discount rate, and escalation rate by using the annual value method. The outcomes of this study show that rebuilding of a pulverized coal-fired boiler with a new one is amortized itself in a very short time.

  9. Low-cost Evaporator Protection Method against Corrosion in a Pulverized Coal Fired Boiler

    Directory of Open Access Journals (Sweden)

    Arkadiusz Krzysztof Dyjakon

    2010-07-01

    Full Text Available Corrosion processes appearing on the watertubes in a combustion chamber of pulverized coal-fired boilers require permanent control and service. Subject to the power plant strategy, different anti-corrosion protection methods can be applied. Technical-economical analysis has been performed to evaluate and support the decisions on maintenance and operation services. The paper presents and discusses results of the application of an air protection system in boiler OP-230 in view of anti-corrosion measures. It is indicated that a low-cost protection method of watertubes (evaporator against corrosion can be efficient and lead to financial savings in comparison to the standard procedure of replacement of watertube panels.

  10. Numerical study of Pavlovskiy coal pulverized combustion in the furnace of BKZ-210-140 steam boiler

    Science.gov (United States)

    Zavorin, A. S.; Gil, A. V.; Khaustov, P. S.; Tabakaev, R. B.; Buslov, D. A.

    2014-10-01

    In this paper pulverized combustion of insufficiently investigated low-grade Pavlovskiy coal is simulated using the modern engineering software FIRE 3D. The object of study is a widespread in Russia BKZ-210-140 steam boiler. The results of computer simulation are represented with average temperatures in horizontal sections and oxygen concentration. Curves are plotted for three steam generating capacity loads of the boiler: 100%, 70% and 50%.

  11. Three Dimensional Modeling of Pulverized Coal combustion in a 600MW Corner Fired Boiler

    Institute of Scientific and Technical Information of China (English)

    SandroDal-Secco

    2000-01-01

    The three-dimensional code ESTET developed at the LNH has been used to predict the reactive flow in a 600 W coal fired boiler,Assuming a no-slip condition between the gas and the coal,the equations for a gas-particle mixture can e written.The pulverized coal particle size distribution is represented by a discrete number of particle size groups determined by the measured fineness distrbution.The combustion models taking into account the pyrolysis of the particle and the heterogeneous combustion of char have been validated using intensive measurements performed on the 600MW utility boiler.Heat fluxes were measured along the walls of the furnace and satisfactory agreement between computation and measurements has been achieved in terms of maximum flux location and heat flux intensity.Local measurements of velocities using LDV probe.gas temperature and gas species concentrations were performed in the vicinity of one burner and compared with the computed variables.Again we have observed a good agreement between the computations and the measurements in terms of jet penetration,temperature distribution.oxygen concentration and ash content.

  12. Renewable wood fuel: Fuel feed system for a pulverized coal boiler. Final report

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1996-01-01

    This report evaluates a pilot test program conducted by New York State Gas & Electric Corporation to evaluate the feasibility of co-firing a pulverized coal plant with renewable wood fuels. The goal was to establish that such a co-firing system can reduce air emissions while maintaining good operational procedures and cost controls. The test fuel feed system employed at Greenidge Station`s Boiler 6 was shown to be effective in feeding wood products. Emission results were promising and an economic analysis indicates that it will be beneficial to pursue further refinements to the equipment and systems. The report recommends further evaluation of the generation and emission impacts using woods of varied moisture contents and at varied Btu input rates to determine if a drying system would be a cost-effective option.

  13. Discussion on Improvement of Chain-grate Boiler to Pulverized Coal Boiler%某链条锅炉改造为煤粉锅炉的探讨

    Institute of Scientific and Technical Information of China (English)

    刘新龙; 王惠云; 杨林; 王鹏南

    2016-01-01

    对链条锅炉改造为煤粉锅炉做了系统的介绍。对改造中所涉及的各系统和设备进行了一定的分析,并证明链条炉改造为煤粉炉是可行的,其配套的烟气处理技术是有效的。%The improvement of the chain-grate boiler to pulverized coal boiler is systematically introduced. Based on the analysis of the related systems and equipments, it's proven that it's feasible to improve the chain-grate boiler to pulverized coal boiler and the corresponding flue gas treatment technology is efficient.

  14. Occurrence and volatility of several trace elements in pulverized coal boiler

    Institute of Scientific and Technical Information of China (English)

    HUANG Ya-ji; JIN Bao-sheng; ZHONG Zhao-ping; XIAO Rui; TANG Zhi-yong; REN Hui-feng

    2004-01-01

    The contents of eight trace elements(Mn, Cr, Pb, As, Se, Zn, Cd, Hg) in raw coal, bottom ash and flyash were measured in a 220 t/h pulverized coal boiler. Factors affecting distribution of trace elements wereinvestigated, including fly ash diameter, furnace temperature, oxygen content and trace elements' characters. Onecoefficient of Meij was also improved to more directly show element enrichment in combustion products. Theseelements may be classified into three groups according to their distribution: Group 1: Hg, which is very volatile.Group 2: Pb, Zn, Cd, which are partially volatile. Group 3: Mn, which is hardly volatile. Se may be locatedbetween groups 1 and 2. Cr has properties of both group 1 and 3. In addition, the smaller diameter of fly ash, themore relative enrichment of trace elements( except Mn). The fly ash showed different adsorption mechanisms oftrace elements and the volatilization of trace elements rises with furnace temperature. Relative enrichments of traceelements(except Mn and Cr) in fly ash are larger than that in bottom ash. Low oxygen content can not alwaysimprove the volatilization of trace elements. Pb is easier to form chloride than Cd during coal combustion. Traceelements should be classified in accordance with factors.

  15. Two-stage numerical simulation for temperature profile in furnace of tangentially fired pulverized coal boiler

    Institute of Scientific and Technical Information of China (English)

    ZHOU Nai-jun; XU Qiong-hui; ZHOU Ping

    2005-01-01

    Considering the fact that the temperature distribution in furnace of a tangential fired pulverized coal boiler is difficult to be measured and monitored, two-stage numerical simulation method was put forward. First, multi-field coupling simulation in typical work conditions was carried out off-line with the software CFX-4.3, and then the expression of temperature profile varying with operating parameter was obtained. According to real-time operating parameters, the temperature at arbitrary point of the furnace can be calculated by using this expression. Thus the temperature profile can be shown on-line and monitoring for combustion state in the furnace is realized. The simul-ation model was checked by the parameters measured in an operating boiler, DG130-9.8/540. The maximum of relative error is less than 12% and the absolute error is less than 120 ℃, which shows that the proposed two-stage simulation method is reliable and able to satisfy the requirement of industrial application.

  16. Experimental study on cement clinker co-generation in pulverized coal combustion boilers of power plants.

    Science.gov (United States)

    Wang, Wenlong; Luo, Zhongyang; Shi, Zhenglun; Cen, Kefa

    2006-06-01

    The idea to co-generate cement clinker in pulverized coal combustion (PCC) boilers of power plants is introduced and discussed. An experimental study and theoretical analysis showed this idea to be feasible and promising. By adding quick lime as well as other mineralizers to the coal and grinding the mixture before combustion, sulfoaluminate cement clinker with a high content of silicate (SCCHS) could be generated. The main mineral phases in SCCHS are 2CaO x SiO2 (dicalcium-silicate), 3CaO x 3Al2O3 x CaSO4 (calcium-sulfoaluminate) and 2CaO x A12O3 SiO2 (gehlenite). Performance tests showed that the SCCHS met the requirements for utilization in common construction. Based on this idea, zero solid waste generation from PCC would be realized. Furthermore, thermal power production and cement production could be combined, and this would have a significant effect on both environmental protection and natural resource saving.

  17. A numerical study of pulverized coal ignition by means of plasma torches in air-coal dust mixture ducts of utility boiler furnaces

    Energy Technology Data Exchange (ETDEWEB)

    Belosevic, S.; Sijercic, M.; Stefanovic, P. [Institute for Nuclear Science Vinca, Belgrade (Serbia)

    2008-04-15

    Paper presents selected results of numerical simulation of processes in air-coal dust mixture duct of pulverized coal utility boiler furnace with plasma-system for pulverized coal ignition and combustion stabilization. Application of the system in utility boiler furnaces promises to achieve important savings compared with the use of heavy oil burners. Plasma torches are built in air-coal dust mixture ducts between coal mills and burners. Calculations have been performed for one of rectangular air-coal dust mixture ducts with two opposite plasma torches, used in 210 MWe utility boiler firing pulverized Serbian lignite. The simulations are based on a three-dimensional mathematical model of mass, momentum and heat transfer in reacting turbulent gas-particle flow, specially developed for the purpose. Characteristics of processes in the duct are analyzed in the paper, with respect to the numerical results. The plasma-system thermal effect is discussed as well, regarding corresponding savings of liquid fuel. It has been emphasized that numerical simulation of the processes can be applied in optimization of pulverized coal ignition and combustion stabilization and enables efficient and cost-effective scaling-up procedure from laboratory to industrial scale.

  18. 工业煤粉锅炉控制系统的开发及应用%Development and application of industrial pulverized coal boiler control system

    Institute of Scientific and Technical Information of China (English)

    麻林

    2014-01-01

    With the promotion of energy saving and environmental protection, improve the industrial boiler thermal efficiency is one of the most important parts, small and medium-sized industrial pulverized coal boiler is developed in recent years is more efficient coal-fired industrial boilers, the boiler of 200μm pulverized coal combustion stability has a very high demand, while new auxiliary unit. According to the characteristics of the pulverized coal boiler, developed a set of pulverized coal boiler con-trol system. The characteristics of the control system mainly includes additional storage, powder, powder supply control, combus-tion control and diagnosis of combustion control, to ensure the safe, stable, efficient pulverized coal boiler operation.%随着近几年节能环保的提倡,提高工业锅炉热效率是其中重要的部分,中小型工业煤粉锅炉是近几年出现的较为高效的燃煤工业锅炉,该锅炉对200目煤粉的稳定燃烧有很高的要求,同时新增辅机配套单元。针对工业煤粉锅炉的特点,开发了一套工业煤粉锅炉控制系统。该控制系统特点主要有:储粉、供粉控制、煤粉燃烧控制和燃烧诊断控制,从而保障了工业煤粉锅炉安全、稳定、高效的运行。

  19. Mercury speciation and its emissions from a 220 MW pulverized coal-fired boiler power plant in flue gas

    Energy Technology Data Exchange (ETDEWEB)

    Yang, X.H.; Zhuo, Y.Q.; Duan, Y.F.; Chen, L.; Yang, L.G.; Zhang, L.A.; Jiang, Y.M.; Xu, X.C. [Southeast University, Nanjing (China). Thermoenergy Engineering Research Institute

    2007-07-15

    Distributions of mercury speciation of Hg{sup 0}, Hg{sup 2+} and Hg{sup P} in flue gas and fly ash were sampled by using the Ontario Hydro Method in a 220 MW pulverized coal-fired boiler power plant in China. The mercury speciation was varied greatly when flue gas going through the electrostatic precipitator (ESP). The mercury adsorbed on fly ashes was found strongly dependent on unburnt carbon content in fly ash and slightly on the particle sizes, which implies that the physical and chemical features of some elemental substances enriched to fly ash surface also have a non-ignored effect on the mercury adsorption. The concentration of chlorine in coal, oxygen and NOx in flue gas has a positive correlation with the formation of the oxidized mercury, but the sulfur in coal has a positive influence on the formation of elemental mercury.

  20. PROTOTYPE SCALE TESTING OF LIMB TECHNOLOGY FOR A PULVERIZED-COAL-FIRED BOILER

    Science.gov (United States)

    The report summarizes results of an evaluation of furnace sorbent injection (FSI) to control sulfur dioxide (SO2) emissions from coal-fired utility boilers. (NOTE: FSI of calcium-based sorbents has shown promise as a moderate SO2 removal technology.) The Electric Power Research I...

  1. Effect of Particle Size Distribution on Wall Heat Flux in Pulverized-Coal Furnaces and Boilers

    Science.gov (United States)

    Lu, Jun

    A mathematical model of combustion and heat transfer within a cylindrical enclosure firing pulverized coal has been developed and tested against two sets of measured data (one is 1993 WSU/DECO Pilot test data, the other one is the International Flame Research Foundation 1964 Test (Beer, 1964)) and one independent code FURN3D from the Argonne National Laboratory (Ahluwalia and IM, 1992). The model called PILC assumes that the system is a sequence of many well-stirred reactors. A char burnout model combining diffusion to the particle surface, pore diffusion, and surface reaction is employed for predicting the char reaction, heat release, and evolution of char. The ash formation model included relates the ash particle size distribution to the particle size distribution of pulverized coal. The optical constants of char and ash particles are calculated from dispersion relations derived from reflectivity, transmissivity and extinction measurements. The Mie theory is applied to determine the extinction and scattering coefficients. The radiation heat transfer is modeled using the virtual zone method, which leads to a set of simultaneous nonlinear algebraic equations for the temperature field within the furnace and on its walls. This enables the heat fluxes to be evaluated. In comparisons with the experimental data and one independent code, the model is successful in predicting gas temperature, wall temperature, and wall radiative flux. When the coal with greater fineness is burnt, the particle size of pulverized coal has a consistent influence on combustion performance: the temperature peak was higher and nearer to burner, the radiation flux to combustor wall increased, and also the absorption and scattering coefficients of the combustion products increased. The effect of coal particle size distribution on absorption and scattering coefficients and wall heat flux is significant. But there is only a small effect on gas temperature and fuel fraction burned; it is speculated

  2. Investigation of the flow, combustion, heat-transfer and emissions from a 609MW utility tangentially fired pulverized-coal boiler

    DEFF Research Database (Denmark)

    Yin, Chungen; Caillat, Sébastien; Harion, Jean-Luc.;

    2002-01-01

    A numerical approach is given to investigate the performance of a 609 MW tangentially fired pulverized-coal boiler, with emphasis on formation mechanism of gas flow deviation and uneven wall temperature in crossover pass and on NOx emission. To achieve this purpose and obtain a reliable solution...... are reliable. These conclusions can be used to guide the design and operation of boilers of similar types....

  3. Modelling of pulverized coal boilers: review and validation of on-line simulation techniques

    Energy Technology Data Exchange (ETDEWEB)

    Diez, L.I.; Cortes, C.; Campo, A. [University of Zaragoza, Zaragoza (Spain). Centro de Investigacion de Recursos y Consumos Energeticos (CIRCE)

    2005-07-01

    Thermal modelling of large pulverized fuel utility boilers has reached a very remarkable development, through the application of CFD techniques and other advanced mathematical methods. However, due to the computational requirements, on-line monitoring and simulation tools still rely on lumped models and semiempirical approaches, which are often strongly simplified and not well connected with sound theoretical basis. This paper reviews on-line modelling techniques, aiming at the improvement of their capabilities, by means of the revision and modification of conventional lumped models and the integration of off-line CFD predictions. The paper illustrates the coherence of monitoring calculations as well as the validation of the on-line thermal simulator, starting from real operation data from a case-study unit. The outcome is that it is possible to significantly improve the accuracy of on-line calculations provided by conventional models, taking into account the singularities of large combustion systems and coupling offline CFD predictions for selected scenarios.

  4. Assessing the Exergy Costs of a 332-MW Pulverized Coal-Fired Boiler

    Directory of Open Access Journals (Sweden)

    Victor H. Rangel-Hernandez

    2016-08-01

    Full Text Available In this paper, we analyze the exergy costs of a real large industrial boiler with the aim of improving efficiency. Specifically, the 350-MW front-fired, natural circulation, single reheat and balanced draft coal-fired boiler forms part of a 1050-MW conventional power plant located in Spain. We start with a diagram of the power plant, followed by a formulation of the exergy cost allocation problem to determine the exergy cost of the product of the boiler as a whole and the expenses of the individual components and energy streams. We also define a productive structure of the system. Furthermore, a proposal for including the exergy of radiation is provided in this study. Our results show that the unit exergy cost of the product of the boiler goes from 2.352 to 2.5, and that the maximum values are located in the ancillary electrical devices, such as induced-draft fans and coil heaters. Finally, radiation does not have an effect on the electricity cost, but affects at least 30% of the unit exergy cost of the boiler’s product.

  5. The application of RANS CFD for design of SNCR technology for a pulverized coal-fired boiler

    Directory of Open Access Journals (Sweden)

    Ruszak Monika

    2017-06-01

    Full Text Available The article describes the technology of NOx emission abatement by SNCR method. The scope of research included CDF simulations as well as design and construction of the pilot plant and tests of NOx reduction by urea in the plant located in industrial pulverized-coal fired boiler. The key step of research was to determine the appropriate temperature window for the SNCR process. The proposed solution of the location of injection lances in the combustion chamber enabled to achieve over a 30% reduction of NOx. It is possible to achieve higher effectiveness of the proposed SNCR technology and meet the required emission standards via providing prior reduction of NOx to the level of 350 mg/um3 using the primary methods.

  6. Investigation of Fly Ash and Activated Carbon Obtained from Pulverized Coal Boilers

    Energy Technology Data Exchange (ETDEWEB)

    Edward K. Levy; Christopher Kiely; Zheng Yao

    2006-08-31

    One of the techniques for Hg capture in coal-fired boilers involves injection of activated carbon (AC) into the boiler downstream of the air preheater. Hg is adsorbed onto the AC particles and fly ash, which are then both removed in an electrostatic precipitator or baghouse. This project addressed the issues of Hg on activated carbon and on fly ash from a materials re-use point of view. It also addressed the possible connection between SCR reactors, fly ash properties and Hg capture. The project has determined the feasibility of separating AC from fly ash in a fluidized bed and of regenerating the separated AC by heating the AC to elevated temperatures in a fluidized bed. The temperatures needed to drive off the Hg from the ash in a fluidized bed have also been determined. Finally, samples of fly ash from power plants with SCR reactors for NO{sub x} control have been analyzed in an effort to determine the effects of SCR on the ash.

  7. The applicability analysis of burning Indonesian coal in small efficient pulverized coal fired boiler%小型高效煤粉锅炉燃用印尼煤的适用性分析

    Institute of Scientific and Technical Information of China (English)

    王忠会; 马文静; 李会强; 马维唯

    2015-01-01

    结合高效煤粉锅炉的工艺流程、技术特点及印尼煤的煤质分析,探讨了小型高效煤粉锅炉燃用印尼煤的适用性分析。由小型工业煤粉锅炉燃用印尼煤的实际运行结果可知,可选择适合小型煤粉锅炉燃用的印尼煤燃料,以确保锅炉的正常运行。%The applicability analysis of burning Indonesian coal in small efficient pulverized coal fired boiler was done combined with efficient pulverized coal fired boiler process flow,technical features and coal quality analysis of the Indonesian coal.The practical operating results of small efficient pulverized coal fired boiler burning Indonesian coal showed that choosing the suitable Indonesian coal could ensure the normal operation of the boiler.

  8. Numerical analysis of loads effect on combustion performance and NO{sub x} emissions of a 220 MW pulverized coal boiler

    Energy Technology Data Exchange (ETDEWEB)

    Li, Jun; Yang, Weihong; Blasiak, Wlodzimierz [Royal Institute of Technology (KTH), Stockholm (Sweden). Div. of Energy and Furnace Technology; Jankowski, Radoslaw; Kotecki, Michal; Szewczyk, Dariusz [Industrial Combustion Systems (ICS) Company, Poznan (Poland); Brzdekiewicz, Artur [Remak-Rozruch SA, Opole (Poland)

    2013-07-01

    This paper presents numerical study on the combustion performance and NO{sub x} emissions of a 220 MW pulverized coal boiler. Three different loads have been simulated with combusting coal, 200, 170 and 140 MW, respectively. In order to get as precise as possible numerical analysis results, two-step simulation method has been adopted in this work, namely, air supply system simulation and furnace simulation. After air supply system simulation, the results have been taken as the initial and boundary conditions for furnace simulation. The comparison between the measured values and predicted results from 200 MW case shows much better agreement. According to the simulation results, the adopted two-step simulation method is reasonable and suitable for predicting the characters of the flow and combustion process. It is concluded that the distributions of temperature, O{sub 2} and CO concentration inside furnace with different loads shows good similarly. The total NOx emissions decreased with the boiler load reducing, and fuel NO{sub x} has the same trend as total NO{sub x}, and fuel NO{sub x} account for about 66% in total NO{sub x} in all the three cases. More important, thermal NO{sub x} slowly decreased with the rise of boiler load. More detailed results presented in this paper enhance the understanding of combustion processes and complex flow patterns of front-wall pulverized coal boilers.

  9. Coal char fragmentation during pulverized coal combustion

    Energy Technology Data Exchange (ETDEWEB)

    Baxter, L.L.

    1995-07-01

    A series of investigations of coal and char fragmentation during pulverized coal combustion is reported for a suite of coals ranging in rank from lignite to low-volatile (lv) bituminous coal under combustion conditions similar to those found in commercial-scale boilers. Experimental measurements are described that utilize identical particle sizing characteristics to determine initial and final size distributions. Mechanistic interpretation of the data suggest that coal fragmentation is an insignificant event and that char fragmentation is controlled by char structure. Chars forming cenospheres fragment more extensively than solid chars. Among the chars that fragment, large particles produce more fine material than small particles. In all cases, coal and char fragmentation are seen to be sufficiently minor as to be relatively insignificant factors influencing fly ash size distribution, particle loading, and char burnout.

  10. JV Task 106 - Feasibility of CO2 Capture Technologies for Existing North Dakota Lignite-Fired Pulverized Coal Boilers

    Energy Technology Data Exchange (ETDEWEB)

    Michael L. Jones; Brandon M. Pavlish; Melanie D. Jensen

    2007-05-01

    The goal of this project is to provide a technical review and evaluation of various carbon dioxide (CO{sub 2}) capture technologies, with a focus on the applicability to lignite-fired facilities within North Dakota. The motivation for the project came from the Lignite Energy Council's (LEC's) need to identify the feasibility of CO{sub 2} capture technologies for existing North Dakota lignite-fired, pulverized coal (pc) power plants. A literature review was completed to determine the commercially available technologies as well as to identify emerging CO{sub 2} capture technologies that are currently in the research or demonstration phase. The literature review revealed few commercially available technologies for a coal-fired power plant. CO{sub 2} separation and capture using amine scrubbing have been performed for several years in industry and could be applied to an existing pc-fired power plant. Other promising technologies do exist, but many are still in the research and demonstration phases. Oxyfuel combustion, a technology that has been used in industry for several years to increase boiler efficiency, is in the process of being tailored for CO{sub 2} separation and capture. These two technologies were chosen for evaluation for CO{sub 2} separation and capture from coal-fired power plants. Although oxyfuel combustion is still in the pilot-scale demonstration phase, it was chosen to be evaluated at LEC's request because it is one of the most promising emerging technologies. As part of the evaluation of the two chosen technologies, a conceptual design, a mass and energy balance, and an economic evaluation were completed.

  11. Clean coal reference plants: Pulverized encoal PDF fired boiler. Topical report

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1995-12-01

    The Clean Coal Technology Demonstration Program (CCT) is a government and industry cofunded technology development effort to demonstrate a new generation of innovative coal utilization processes in a series of full-scale facilities. The goal of the program is to provide the U.S. energy marketplace with a number of advanced, more efficient, and environmentally responsive coal-using technologies. To achieve this goal, a multiphased effort consisting of five separate solicitations has been completed. The Morgantown Energy Technology Center (METC) has the responsibility for monitoring the CCT Projects within certain technology categories, which, in general, correspond to the center`s areas of technology development. Primarily the categories of METC CCT projects are: atmospheric fluid bed combustion, pressurized fluidized bed combustion, integrated gasification combined cycle, mild gasification, and industrial applications. This report describes the plant design.

  12. CFD analysis of the pulverized coal combustion processes in a 160 MWe tangentially-fired-boiler of a thermal power plant

    Energy Technology Data Exchange (ETDEWEB)

    Silva, Cristiano V. da; Beskow, Arthur B. [Universidade Regional Integrada do Alto Uruguai e das Misses (LABSIM/GEAPI/URI), Erechim, RS (Brazil). Dept. de Engenharia e Ciencia da Computacao. Grupo de Engenharia Aplicada a Processos Industriais], Emails: cristiano@uricer.edu.br, Arthur@uricer.edu.br; Indrusiak, Maria Luiza S. [Universidade do Vale do Rio dos Sinos (UNISINOS), Sao Leopoldo, RS (Brazil). Programa de Engenharia Mecanica], E-mail: sperbindrusiak@via-rs.net

    2010-10-15

    The strategic role of energy and the current concern with greenhouse effects, energetic and exegetic efficiency of fossil fuel combustion greatly enhance the importance of the studies of complex physical and chemical processes occurring inside boilers of thermal power plants. The state of the art in computational fluid dynamics and the availability of commercial codes encourage numeric studies of the combustion processes. In the present work the commercial software CFX Ansys Europe Ltd. was used to study the combustion of coal in a 160 MWe commercial thermal power plant with the objective of simulating the operational conditions and identifying factors of inefficiency. The behavior of the flow of air and pulverized coal through the burners was analyzed, and the three-dimensional flue gas flow through the combustion chamber and heat exchangers was reproduced in the numeric simulation. (author)

  13. Numerical study on the impact of varying operation conditions on NOx emissions of large-scale pulverized coal-fired utility boiler

    Energy Technology Data Exchange (ETDEWEB)

    Shen, Yue-yun [Jiangsu Institute of Economic and Trade Technology, Nanjing (China); Gao, Xiao-tao [Jiangsu Electric Power Test and Research CO., LTD, Nanjing (China); Zhang, Ming-yao [Southeast Univ., Nanjing (China). School of Energy and Environment

    2013-07-01

    For complying with the increasingly strengthened regulation on NOx emission from coal fired power plant, newly built large-scale pulverized coal-fired utility boilers are all installed with low-NOx combustion systems to low NOx emissions. Understanding the characteristics of the system is essential for fully utilizing the system without affecting the combustion performance. In the present work, computational fluid dynamics (CFD) approach was applied to simulate the combustion and NOx formation processes in the furnace of 1,000 MW ultra- supercritical boiler equipped with an advanced low-NOx combustion system so as to study the impacts of varying the operation conditions on its NOx emission as well as combustion characteristics. The combustion system is the Mitsubishi Advanced Combustion Technology system consisting of six levels corner-fired pollution minimum (PM) coal burners and additional air to achieve air staging combustion. With the help of CFD simulation, the distributions of the combustion temperature and CO, O{sub 2} and NO concentrations were calculated and analyzed. The main influential operation parameters studied include coal type, additional air flow rate, excess air level and mill groups in service. The CFD simulations indicated that the main reasons of the low NOx emission from this boiler are on two aspects: rationally organizing the combustion process to achieve relatively uniform temperature distribution and reducing combustion environment in the main combustion zone, and combining the utilizations of the large amount of additional air to achieve deep air stage and the low excess air level as well as PM burners. It was also found that varying the operational parameters had considerable effects on the performance of the combustion system.

  14. Optimization Renovation of Low NOx Combustion in Pulverized Coal Fired Boiler of Thermal Power Plant%电厂煤粉锅炉的低氮燃烧优化改造

    Institute of Scientific and Technical Information of China (English)

    常志国

    2012-01-01

    The mechanism for generation of NOx in the combustion process of pulverized coal fired boiler was introduced. Connecting with renovation of pulverized coal fired boiler, the principle of reducing NOx discharge through air classification combustion was introduced, and the experimental result was analyzed and discussed. After air classification combustion renovation, the discharge of NOx from pulverized coal fired boiler decreased substantially, and the main performance indexes of boiler were improved, which achieved good economic profit and environmental protection effects.%阐述了在煤粉锅炉燃烧过程中氮氧化物(NOx)的产生机理和影响因素,结合煤粉锅炉改造,介绍了采用空气分级燃烧降低NOx排放的原理,并对试验结果进行了分析和讨论。实施空气分级燃烧改造后,煤粉锅炉的NOx排放量大幅减少,锅炉的主要性能参数指标得到提升,取得了良好的经济效益和环保效果。

  15. 太阳能在煤粉锅炉上的应用%Application of Solar Energy in Pulverized Coal Boiler

    Institute of Scientific and Technical Information of China (English)

    王春华; 李梦浩; 徐乐乐; 刘小秋; 韩长明; 梁源

    2012-01-01

    Through conducting numerical simulation on the combustion and heat transfer process of the boiler, under the conditions of the different temperature the temperature distribution and volume fraction distribution of the pollutant in the combustion chamber were predicted. The results show that when the furnace temperature met the production requirement if the secondary and tertiary air is preheated to a high - temperature, the total amount of air and coal are both reduced. Meanwhile, the amount of the pollutants could be reduced to achieve the purpose of energy - saving and emissions - reduction. As the increasing air temperature, the furnace temperature at the same section is more uniformity, thus the water wall tube would be heated uniformly, which is helpful for water cycle stability in boiler. Therefore, combustion technology of high temperature and low oxygen could be used in the pulverized coal boiler. To reach high - temperature air, a solar air - heater should be installed on boilers tail to utilize solar energy to assist the flue gas waste heat to heat the secondary and tertiary air to 873 K above.%通过对煤粉锅炉炉膛内的燃烧、传热过程进行数值计算研究,预测了不同空气温度下炉膛内的温度分布和污染物体积分数分布.结果表明,在达到工业生产要求的炉内温度时,二、三次风使用高温空气,可降低总空气量和煤粉消耗量,同时还可减少污染物的生成量,达到节能减排的目的;随着空气温度的升高,炉膛内同一截面的温度更加趋于均匀,这样水冷壁各管吸热均匀,有利于锅炉水循环的稳定性,有利于煤粉锅炉应用高温低氧燃烧技术.为了实现空气高温,可在锅炉尾部增设太阳能空气加热器,利用太阳能辅助烟气余热将二、三次风加热到873 K以上.

  16. 合同能源管理在煤粉工业锅炉岛市场化中的应用%Energy performance contracting in marketization of industrial pulverized coal boiler

    Institute of Scientific and Technical Information of China (English)

    纪任山

    2014-01-01

    为探索煤粉工业锅炉岛的合理经营模式,介绍了合同能源管理( EPC)的基本理论,并以案例从节能效果、其他实际应用效果(减员效果、节能减排效果)、项目经济性及节能效益、风险分析与控制等各方面分析了EPC模式在高效煤粉锅炉中的具体应用和EPC模式为高效煤粉锅炉带来的市场优势。结果表明,EPC模式是适合高效煤粉锅炉市场化推广的有效模式,也为其他高科技节能产品的商业化、产业化提供了成功的案例。组建合同能源管理联盟,为项目参与各方的发展提供良好的交流平台,也是未来的趋势。%In order to explore the reasonable management mode of pulverized coal fired industrial boiler island, introduce the profiles of in-dustrial boilers and the new technology system of pulverized coal industrial boilers island and the basic theory of energy performance con-tracting(EPC).At the same time,the energy saving effects,other practical application effects,economic projects,risk analysis and control of contract in pulverized coal fired boiler in the specific application and EPC model bring to the market advantages of efficient pulverized coal fired boiler were analyzed by cases.The results show that the EPC model is suitable,effective mode for the popularization of efficient pulverized coal boiler,which provides a successful case for the commercialized and industrialized of other high-tech energy-saving prod-ucts.Building an energy performance contracting alliances,which provides a good exchange platform for the development of the parties in-volved in a project,and it is the future trend.

  17. Enhancement of pulverized coal combustion by plasma technology

    Energy Technology Data Exchange (ETDEWEB)

    Gorokhovski, M.A.; Jankoski, Z.; Lockwood, F.C.; Karpenko, E.I.; Messerle, V.E.; Ustimenko, A.B. [University of Rouen, Rouen (France)

    2007-07-01

    Plasma-assisted pulverized coal combustion is a promising technology for thermal power plants (TPP). This article reports one- and three- dimensional numerical simulations, as well as laboratory and industrial measurements of coal combustion using a plasma-fuel system (PFS). The chemical kinetic and fluid mechanics involved in this technology are analysed. The results show that a PFS, can be used to promote early ignition and enhanced stabilization of a pulverized coal flame. It is shown that this technology, in addition to enhancing the combustion efficiency of the flame, reduces harmful emissions from power coals of all ranks (brown, bituminous, anthracite and their mixtures). Data summarising the experience of 27 pulverized coal boilers in 16 thermal power plants in several countries (Russia, Kazakhstan, Korea, Ukraine, Slovakia, Mongolia and China), embracing steam productivities from 75 to 670 tons per hour (TPH), are presented. Finally, the practical computation of the characteristics of the PFS, as function of coal properties, is discussed.

  18. Numerical modelling of lighting process in pulverized-coal burner of a boiler unit by the low-temperature plasma jet

    Energy Technology Data Exchange (ETDEWEB)

    Miloshevich, H.; Rychkov, A.D. [Siberian Branch of Russian Academy of Sciences, Novosibirsk (Russian Federation). Inst. of Occupational Technologies

    1999-07-01

    The authors numerically modelled the process of aeromixture ignition in a pulverized-coal burner by a central axysymmetric jet of air that is heated in an electrical are plasma generator up to about 5000 K. The aim was to investigate the process of coal particle ignition in the flow and establish the conditions under which the independent combustion of pulverized coal mixture occurs. The results obtained showed the important role of radiation heat transfer in initiating the combustion process of solid fuel particles. 8 refs., 5 figs.

  19. Influence of staged-air on airflow, combustion characteristics and NO(x) emissions of a down-fired pulverized-coal 300 MW(e) utility boiler with direct flow split burners.

    Science.gov (United States)

    Li, Zhengqi; Kuang, Min; Zhang, Jia; Han, Yunfeng; Zhu, Qunyi; Yang, Lianjie; Kong, Weiguang

    2010-02-01

    Cold airflow experiments were conducted to investigate the aerodynamic field in a small-scale furnace of a down-fired pulverized-coal 300 MW(e) utility boiler arranged with direct flow split burners enriched by cyclones. By increasing the staged-air ratio, a deflected flow field appeared in the lower furnace; larger staged-air ratios produced larger deflections. Industrial-sized experiments on a full-scale boiler were also performed at different staged-air damper openings with measurements taken of gas temperatures in the burner region and near the right-side wall, wall heat fluxes, and gas components (O(2), CO, and NO(x)) in the near-wall region. Combustion was unstable at staged-air damper openings below 30%. For openings of 30% and 40%, late ignition of the pulverized coal developed and large differences arose in gas temperatures and heat fluxes between the regions near the front and rear walls. In conjunction, carbon content in the fly ash was high and boiler efficiency was low with high NO(x) emission above 1200 mg/m(3) (at 6% O(2) dry). For fully open dampers, differences in gas temperatures and heat fluxes, carbon in fly ash and NO(x) emission decreased yielding an increase in boiler efficiency. The optimal setting is fully open staged-air dampers.

  20. Feasibility of semi coke combustion in industrial pulverized coal boiler%煤粉工业锅炉燃烧兰炭试验研究

    Institute of Scientific and Technical Information of China (English)

    牛芳

    2015-01-01

    In order to burn semi coke in industrial pulverized coal boiler,taking the semi coke produced by Shaanxi Coal and Chemical In-dustry Group as research object,the pulverized coal combustion test in industrial boiler was conducted. The ignition,stable combustion and after-combustion were investigated. The corresponding reform measures were provided. The results showed that,the unique double-cone structure of the combustor and the mode of dense phase combustion provided favorable conditions for the ignition and stable combustion of semi coke. The blue coke could be ignited and burned stably when the excess air coefficient was 1. 2 and the proportion of primary air,sec-ondary air and tertiary air was 0. 11,0. 47,0. 42,the combustor was preheated for 3 minutes and the semi coke burned with oil for 4 mi-nutes. During combustion,the temperature in the back of furnace remained 550 ℃,while the temperature in the middle was over 800 ℃. In order to lower burning point,improve temperature in the fire area and make semi coke full combustion,the structure and size of combus-tor was adjusted,the preheating time was prolonged.%为提高兰炭在煤粉工业锅炉上的燃烧效率,以陕西煤业化工集团生产的兰炭为原料,进行煤粉工业锅炉燃烧试验,分析了兰炭着火、稳燃、燃烬情况;针对兰炭燃烧过程中存在的问题提出解决方案。结果表明:高效煤粉工业锅炉双锥燃烧器的独特结构和浓相燃烧的方式,为兰炭的着火和稳燃提供了良好条件。在过量空气系数1.2,一、二、三次风比例分别为0.11、0.47、0.42,预热时间3 min,伴燃时间4 min的条件下,实现了兰炭粉的着火和自维持稳定燃烧,燃烧期间后部温度保持在550℃,炉膛中部温度大于800℃。针对兰炭燃烧存在燃烧器内燃点靠后、着火区域温度低和兰炭燃烧不完全等问题,提出可通过调整燃烧室的结构和尺寸,使燃烧器蓄热能力增强,

  1. Pulverized Coal Fired Boiler Water Wall Welding Method Exploration%煤粉锅炉水冷壁的焊接方法探究

    Institute of Scientific and Technical Information of China (English)

    李波涛; 江一平; 霍雅洁

    2016-01-01

    During tube header and tube bundle welding of pulverized coal fired boiler water wall tube, sometimes due to improper handling can cause severe wave tube deformation, individual fins seal defects such as cracks. In addition, because of the limitation of space position during welding, the operation is very difficult. In order to ensure the welding quality of tube header and tube bundle, reduce welding defects, more easily to conduct welding operation, a new welding way was designed. And the site-welding experiment for this welding way was carried out. The test results of welding sample showed that this welding method can obtain good effect, and once qualified rate reached 95%.%在煤粉锅炉水冷壁管屏的管集箱和管排焊接时,有时由于处理不当会造成管屏产生波浪变形,个别鳍片出现密封裂纹等缺陷.另外,由于焊接时空间位置的限制,操作相当困难.为了保证管集箱和管排的焊接质量,减少焊接缺陷,更方便地进行焊接操作,设计了一种新型焊接方法,并进行了现场焊接试验.对焊接试样的检测结果表明,该焊接方法可以取得较好的焊接效果,检测一次合格率达到95%.

  2. Plasma system for start-up of pulverized fuel-fired boilers

    Energy Technology Data Exchange (ETDEWEB)

    Dyjakon, A.K. [Wroclaw Univ. of Technology, Wroclaw (Poland). Inst. of Power Engineering and Fluid Mechanics

    2009-07-01

    Pulverized coal combustion requires preliminary heating of the combustion chamber. Conventional heavy oil start-up systems are used during the boiler kindling, resulting in pollution, additional maintenance and high cost. This paper described the advantages of a plasma start-up system for the ignition and stabilization of a pulverized coal flame in coal-fired steam boiler. In a plasma start-up system, the heat source for ignition and stabilization of the pulverized coal combustion is a plasma at a temperature of 5,000 to 10,000 degrees C. The plasma interaction involves rapid heating of coal particles and thermal decomposition of the organic compounds resulting in fast release of the volatile matter and destruction of particles below 5 {mu}m. It also involves thermal dissociation of gaseous products with radical generation and gas ionization. The highly reactive mixture that is produced promotes flame propagation in the presence of oxygen. A continuous plasma discharge in a pulverized burner stabilizes the dust flame. This paper described the advantages associated with the use of a plasma start-up system, such as the possibility of limiting pollutant emissions to the atmosphere. It also presented laboratory study results on the influence of the fuels such as lignite, bituminous coal, wood and carbonaceous shale and their properties on the operational range of the plasma assisted pulverized coal burner. 13 refs., 2 tabs., 7 figs.

  3. Numerical Simulation of Combustion Characteristics of a 300 MW Blast Furnace Gas/Pulverized Coal Combined Combustion Boiler%300MW煤粉/高炉煤气混燃锅炉燃烧特性数值模拟

    Institute of Scientific and Technical Information of China (English)

    王春波; 魏建国; 盛金贵; 李艳奇

    2012-01-01

    Blast furnace gas(BFG) produced from steel mill is a low heat value fuel,which combined with pulverized coal to combust in boiler is one of effective ways.However,the combustion characteristics would be changed greatly when compared with only pulverized coal combustion.For example,superheaters and reheaters are easy to excess rated temperatures and carbon content in fly ash will become higher,etc.All these problems lead to its limited application today.Take a 300MW BFG/pulverized coal boiler for example,the combustion characteristics were simulated by means of two mixture fractions way.The pure coal condition and three BFG ratio: 10%,20% and 30% conditions were investigated.It shows the temperature level in boiler is lowered obviously when BFG was mixed into boiler.For example,the maximal temperature is lowered about 81K when BFG ratio is 10% for a boiler section.Also,the temperature becomes lower with the BFG ratio.When BFG was mixed into boiler the flue gases volume would be increased.So,the actual stay time for pulverized coal in boiler will be shortened and it is more difficulty for coal to combust completely.Aslo,it is helpfully for control NO emission when BFG was mixed into boiler.%钢厂高炉煤气是一种低热值燃料,它和煤粉在炉内掺烧是其一种有效的利用途径。但煤粉掺烧高炉煤气后燃烧特性与纯煤粉燃烧有很大不同,掺烧过程中易发生过/再热器超温、飞灰含碳量过高等问题,导致其在大型锅炉上的应用很少。针对某钢厂300MW四角切圆煤粉/高炉煤气混燃锅炉,使用二混合分数法对其燃烧特性进行数值模拟。对比研究了纯燃煤工况和高炉煤气掺烧量分别为10%、20%、30%的工况,发现掺烧高炉煤气时炉内温度水平有明显下降(如,掺烧10%高炉煤气时截面最高温度降低81K),且随着掺烧量的增加而加剧,但下降的趋势变缓。掺烧高炉煤气后产生烟气量增多,炉膛出口烟速有明显增加,

  4. Simulation of low-temperature plasma interaction with pulverized coal for incineration improvement

    Energy Technology Data Exchange (ETDEWEB)

    A. Askarova; E. Karpenko; V. Messerle; A. Ustimenko [Al-Farabi Kazakh National University, Almaty (Kazakhstan). Department of Physics

    2003-07-01

    Plasma activation promotes more effective and environmental friendly low-grade coals incineration. The work presents numerical modeling results of plasma ignition, gasification and thermochemical preparation of a pulverized coal for incineration at power boilers. Thermodynamic code TERRA allows calculating products compound of plasma activated pulverized coal depended on temperature, pressure and plasma source power. Considering plasma source kinetic code PLASMA-COAL gives initial data for 3D-modeling of power boilers furnaces by FLOREAN code. 5 refs., 13 figs., 5 tabs.

  5. Cofiring coal-water slurry fuel with pulverized coal as a NOx reduction strategy

    Energy Technology Data Exchange (ETDEWEB)

    Miller, B.G.; Miller, S.F.; Morrison, J.L.; Scaroni, A.W. [Pennsylvania State Univ., University Park, PA (United States)

    1997-12-31

    A low solids, low viscosity coal-water slurry fuel (CWSF) was formulated and produced from impounded bituminous coal fines and burned in a utility-scale boiler to investigate NOx emissions reduction during the cofiring of CWSF with pulverized coal. Tests were conducted at the Pennsylvania Electric Company (Penelec) Seward Station, located near Seward, Pennsylvania in a Babcock and Wilcox (B and W), front-wall fired, pulverized coal boiler (34 MWe). Two B and W pulverizers feed coal to six burners (two burner levels each containing three low-NOx burners). Approximately 20% of the thermal input was provided by CWSF, the balance by pulverized coal. There was a significant reduction of NOx emissions when cofiring CWSF and pulverized coal as compared to firing 100% pulverized coal. The level of reduction was dependent upon the cofiring configuration (i.e., cofiring in the upper three, lower three, or all six burners), with NOx emissions being reduced by as much as 26.5%. The reduction in NOx emissions was not due to the tempering effect of the water in the CWSF, because a greater reduction in NOx occurred when cofiring CWSF than when injecting the same quantity of water at the same boiler firing rate. This paper discusses the tests in detail and the proposed reburn mechanism for the NOx reduction. In addition, combustion test results from the front-wall fired unit at the Seward Station will be compared to CWSF cofire tests that have been conducted at cyclone-fired units at Tennessee Valley Authority`s (TVA) Paradise Station (704 MWe), Drakesboro, Kentucky and Southern Illinois Power Cooperative`s (SIPC) Marion, Illinois Station (33 MWe).

  6. Enhanced Combustion Low NOx Pulverized Coal Burner

    Energy Technology Data Exchange (ETDEWEB)

    David Towle; Richard Donais; Todd Hellewell; Robert Lewis; Robert Schrecengost

    2007-06-30

    For more than two decades, Alstom Power Inc. (Alstom) has developed a range of low cost, infurnace technologies for NOx emissions control for the domestic U.S. pulverized coal fired boiler market. This includes Alstom's internally developed TFS 2000{trademark} firing system, and various enhancements to it developed in concert with the U.S. Department of Energy. As of the date of this report, more than 270 units representing approximately 80,000 MWe of domestic coal fired capacity have been retrofit with Alstom low NOx technology. Best of class emissions range from 0.18 lb/MMBtu for bituminous coal to 0.10 lb/MMBtu for subbituminous coal, with typical levels at 0.24 lb/MMBtu and 0.13 lb/MMBtu, respectively. Despite these gains, NOx emissions limits in the U.S. continue to ratchet down for new and existing boiler equipment. On March 10, 2005, the Environmental Protection Agency (EPA) announced the Clean Air Interstate Rule (CAIR). CAIR requires 25 Eastern states to reduce NOx emissions from the power generation sector by 1.7 million tons in 2009 and 2.0 million tons by 2015. Low cost solutions to meet such regulations, and in particular those that can avoid the need for a costly selective catalytic reduction system (SCR), provide a strong incentive to continue to improve low NOx firing system technology to meet current and anticipated NOx control regulations. The overall objective of the work is to develop an enhanced combustion, low NOx pulverized coal burner, which, when integrated with Alstom's state-of-the-art, globally air staged low NOx firing systems will provide a means to achieve: Less than 0.15 lb/MMBtu NOx emissions when firing a high volatile Eastern or Western bituminous coal, Less than 0.10 lb/MMBtu NOx emissions when firing a subbituminous coal, NOx reduction costs at least 25% lower than the costs of an SCR, Validation of the NOx control technology developed through large (15 MWt) pilot scale demonstration, and Documentation required for

  7. USE OF COAL DRYING TO REDUCE WATER CONSUMED IN PULVERIZED COAL POWER PLANTS

    Energy Technology Data Exchange (ETDEWEB)

    Edward Levy; Harun Bilirgen; Ursla Levy; John Sale; Nenad Sarunac

    2006-01-01

    This is the twelfth Quarterly Report for this project. The background and technical justification for the project are described, including potential benefits of reducing fuel moisture using power plant waste heat, prior to firing the coal in a pulverized coal boiler. During this last Quarter, the development of analyses to determine the costs and financial benefits of coal drying was continued. The details of the model and key assumptions being used in the economic evaluation are described in this report and results are shown for a drying system utilizing a combination of waste heat from the condenser and thermal energy extracted from boiler flue gas.

  8. USE OF COAL DRYING TO REDUCE WATER CONSUMED IN PULVERIZED COAL POWER PLANTS

    Energy Technology Data Exchange (ETDEWEB)

    Edward Levy; Harun Bilirgen; Ursla Levy; John Sale; Nenad Sarunac

    2006-01-01

    This is the twelfth Quarterly Report for this project. The background and technical justification for the project are described, including potential benefits of reducing fuel moisture using power plant waste heat, prior to firing the coal in a pulverized coal boiler. During this last Quarter, the development of analyses to determine the costs and financial benefits of coal drying was continued. The details of the model and key assumptions being used in the economic evaluation are described in this report and results are shown for a drying system utilizing a combination of waste heat from the condenser and thermal energy extracted from boiler flue gas.

  9. Plasma-supported coal combustion in boiler furnace

    Energy Technology Data Exchange (ETDEWEB)

    Askarova, A.S.; Karpenko, E.I.; Lavrishcheva, Y.I.; Messerle, V.E.; Ustimenko, A.B. [Kazakh National University, Alma Ata (Kazakhstan). Dept. of Physics

    2007-12-15

    Plasma activation promotes more effective and environmentally friendly low-rank coal combustion. This paper presents Plasma Fuel Systems that increase the burning efficiency of coal. The systems were tested for fuel oil-free start-up of coal-fired boilers and stabilization of a pulverized-coal flame in power-generating boilers equipped with different types of burners, and burning all types of power-generating coal. Also, numerical modeling results of a plasma thermochemical preparation of pulverized coal for ignition and combustion in the furnace of a utility boiler are discussed in this paper. Two kinetic mathematical models were used in the investigation of the processes of air/fuel mixture plasma activation: ignition and combustion. A I-D kinetic code PLASMA-COAL calculates the concentrations of species, temperatures, and velocities of the treated coal/air mixture in a burner incorporating a plasma source. The I-D simulation results are initial data for the 3-D-modeling of power boiler furnaces by the code FLOREAN. A comprehensive image of plasma-activated coal combustion processes in a furnace of a pulverized-coal-fired boiler was obtained. The advantages of the plasma technology are clearly demonstrated.

  10. Observer-Based Fuel Control Using Oxygen Measurement. A study based on a first-principles model of a pulverized coal fired Benson Boiler

    Energy Technology Data Exchange (ETDEWEB)

    Andersen, Palle; Bendtsen, Jan Dimon; Mortensen, Jan Henrik; Just Nielsen, Rene; Soendergaard Pedersen, Tom [Aalborg Univ. (Denmark). Dept. of Control Engineering

    2005-01-01

    This report describes an attempt to improve the existing control of coal mills used at the Danish power plant Nordjyllandsvaerket Unit 3. The coal mills pulverize raw coal to a fine-grained powder, which is injected into the furnace of the power plant. In the furnace the coal is combusted, producing heat, which is used for steam production. With better control of the coal mills, the power plant can be controlled more efficiently during load changes, thus improving the overall availability and efficiency of the plant. One of the main difficulties from a control point of view is that the coal mills are not equipped with sensors that detect how much coal is injected into the furnace. During the project, a fairly detailed, non-linear differential equation model of the furnace and the steam circuit was constructed and validated against data obtained at the plant. It was observed that this model was able to capture most of the important dynamics found in the data. Based on this model, it is possible to extract linearized models in various operating points. The report discusses this approach and illustrates how the model can be linearized and reduced to a lower-order linear model that is valid in the vicinity of an operating point by removing states that have little influence on the overall response. A viable adaptive control strategy would then be to design controllers for each of these simplified linear models, i.e., the control loop that sets references to the coal mills and feedwater, and use the load as a separate input to the control. The control gains should then be scheduled according to the load. However, the variations and uncertainties in the coal mill are not addressed directly in this approach. Another control approach was taken in this project, where a Kalman filter based on measurements of air flow blown into the furnace and the oxygen concentration in the flue gas is designed to estimate the actual coal flow injected into the furnace. With this estimate

  11. Engineering and organizational solutions for improvement of engineering and economic characteristics of the TPE-216 boilers equipped with MV-3300/800/490 pulverizing fans

    Science.gov (United States)

    Kirillov, M. V.; Safronov, P. G.

    2014-07-01

    Efficiency of coal-fired boilers is determined in many respects by optimal operation of the coal-pulverizing plants that are increasingly frequently equipped with pulverizing fans. By an example of retrofitted MV-3300/800/490 pulverizing fans, the effects of different factors on the performance and economic efficiency of the coal-pulverizing plants are analyzed. The experience gained in retrofitting MV-3300/800/490 pulverizing fans by introducing the three-crusher operation mode of a TPE-216 boiler employing the internal recirculation and a blading device in the classifier was also studied. Optimization of the boiler's operation mode was made when switching over from the four-crusher to the three-crusher mode, which considerably improved the engineering and economic characteristics.

  12. Pushing the pulverized coal envelope with LEBS

    Energy Technology Data Exchange (ETDEWEB)

    Regan, J.W.; Borio, R.W.; Palkes, M. [and others

    1995-11-01

    In response to challenges from technologies such as IGCC and PFBC, the ABB LEBS Team has proposed removing the barriers to very large advances in environmental and thermal performance of pulverized coal plants. Pulverized coal will continue to be the source of more than half of our electric generation well into the next century and we must develop low-risk low-cost advances that will compete with the claimed performance of other technologies. This paper describes near-term PC technologies for new and retrofit applications which will accomplish this.

  13. Experimental study on operation optimization of the gas/pulverized coal blended combustion boiler%钢厂煤气混烧锅炉运行优化的试验研究

    Institute of Scientific and Technical Information of China (English)

    易正明; 肖慧; 杜炳旭

    2014-01-01

    An experiment was carried out of the adjustment of blast furnace gas (BFG) and coke oven gas (COG) for blended combustion in a gas/pulverized coal blended combustion boiler and analysis was made of the effect of BFG-COG blended combustion on exhaust gas temperature ,fly ash carbon content and superheated steam temperature of the boiler .On this basis ,the boiler operation was opti-mized .The results show that when BFG blending ratio is 30% and COG blending ratio is 40% ,the thermal efficiency of the boiler reaches 80 .9% .This not only guarantees a high thermal efficiency but also achieves a greater proportion blending combustion of BFG ,offering a solution to the problem of excessive BFG and proving to be more economic .%对某钢厂煤气混烧锅炉进行高炉煤气和焦炉煤气掺烧调整试验,分析掺烧对锅炉排烟温度、飞灰含碳量和过热蒸汽温度等的影响,并对锅炉运行进行了优化。结果表明,当高炉煤气掺烧热值比为30%且焦炉煤气掺烧热值比为40%时,锅炉热效率达到80.9%,这样既保证了锅炉较高的热效率,又实现了高炉煤气的较大比例掺烧,解决了其大量过剩问题,具有较好的经济性。

  14. Design and implementation of remote monitoring software for pulverized coal parameters in power station boiler%电站锅炉煤粉参数远程监控系统的软件设计与实现

    Institute of Scientific and Technical Information of China (English)

    胡昌镁; 何渊; 杨斌; 蔡小舒

    2015-01-01

    Online monitoring of pulverized coal in boiler provides the importance reference for optimal control of power station boiler.In order to realize the remote monitoring of particle size,concentration,and velocity of pulverized coal,the upper-computer software of data acquisition system was designed by using modular program design method.This software could realize the system configuration,real-time curve and histogram displaying, data storage,and so on.Each data acquisition and processing channel with 1 MHz sampling frequency was achieved by using multi-thread technology and automatic allocation simultaneously.The capability of real-time communication with the Distributed Control System (DCS)based on the Modbus communication protocol was achieved.The practical runs shown high stability and reliability of this software.And it could meet the demands of operation and optimizing control of boiler well.%电站锅炉煤粉颗粒参数在线监控对于锅炉优化控制有着重要的参考作用。为了实现煤粉管道内颗粒的细度、浓度、速度的实时监控,通过模块化的程序设计方案,设计了数据采集系统的上位机软件。该软件通过自定义控件实现了系统组态、实时曲线与柱状图数据显示、保存等功能。同时利用多线程和通道自动分配方法实现了单通道采样频率达1 MHz 的数据快速采集与处理,并基于 Modbus 通讯协议实现了与 DCS (Distributed Control System)的即时通讯。在电站长时间投入运行的结果表明,该系统具有良好的稳定性与可靠性,各项功能均满足锅炉运行与优化控制要求。

  15. Thermodynamic Characteristics and Economic Analysis of a BFG/Pulverized Coal Mixed Combustion Boiler%300MW高炉煤气与煤粉混燃锅炉热力特性及经济性分析

    Institute of Scientific and Technical Information of China (English)

    王春波; 魏建国; 黄江城

    2012-01-01

    针对高炉煤气与煤粉混燃易发生过(再)热器超温、飞灰含碳量高等问题,对某300MW机组四角切圆高炉煤气/煤粉混燃锅炉进行了热力特性计算,并对掺烧高炉煤气后机组的经济性进行了分析.结果表明:掺烧高炉煤气后炉内温度降低,烟气量增加,辐射吸热量减少而对流吸热量增加,炉膛出口烟温及其后受热面区域的烟温升高,排烟温度升高,锅炉效率降低;掺烧高炉煤气后厂用电率有所升高,但发电煤耗降低,使发电成本降低.%To solve the problems occurring in a 300 MW tangential blast furnace gas (BFG)/pulverized coal blended combustion boiler, such as overheating of its superheater/reheater and high carbon content in the fly ash, etc. , thermodynamic calculations and an economic analysis were carried out. Results show that af- ter the fuel coal is blended with BFG, the in-furnace temperature drops, the exhaust gas volume rises, the absorption of radiation heat reduces, the absorption of convection heat increases, the gas temperatures at and after furnace outlet rise, the exhaust gas temperature increases and the boiler efficiency decreases; af- ter mixing with BFG, the house power consumption rises, but the coal consumption for power generation reduces, which helps to reduce the power generating cost.

  16. Burnout of pulverized biomass particles in large scale boiler - Single particle model approach

    Energy Technology Data Exchange (ETDEWEB)

    Saastamoinen, Jaakko; Aho, Martti; Moilanen, Antero [VTT Technical Research Centre of Finland, Box 1603, 40101 Jyvaeskylae (Finland); Soerensen, Lasse Holst [ReaTech/ReAddit, Frederiksborgsveij 399, Niels Bohr, DK-4000 Roskilde (Denmark); Clausen, Soennik [Risoe National Laboratory, DK-4000 Roskilde (Denmark); Berg, Mogens [ENERGI E2 A/S, A.C. Meyers Vaenge 9, DK-2450 Copenhagen SV (Denmark)

    2010-05-15

    Burning of coal and biomass particles are studied and compared by measurements in an entrained flow reactor and by modelling. The results are applied to study the burning of pulverized biomass in a large scale utility boiler originally planned for coal. A simplified single particle approach, where the particle combustion model is coupled with one-dimensional equation of motion of the particle, is applied for the calculation of the burnout in the boiler. The particle size of biomass can be much larger than that of coal to reach complete burnout due to lower density and greater reactivity. The burner location and the trajectories of the particles might be optimised to maximise the residence time and burnout. (author)

  17. Plasma-fuel systems for environment and economy indexes of pulverized coal incineration and gasification improvement

    Energy Technology Data Exchange (ETDEWEB)

    E. Karpenko; V. Messerle; A. Ustimenko [United Power System of Russia, Gusinoozersk (Russian Federation). Branch Centre of Plasma-Power Technologies of Russian J.S.Co.

    2003-07-01

    Coal is one of the main energy resources. To improve efficiency of coal incineration new plasma-energy technologies are developing. Steam-productivity 75t/h 670t/h boilers were tested for their starting up by plasma ignition of pulverized coal and flame stabilization. Laboratory (coal consumption to 20kg/h) and pilot (coal consumption 300kg/h and 32000kg/h) plasma gasification experiments are given. Plasma air and steam gasification of coal with its mineral mass utilization is studied. 8 refs., 10 figs., 4 tabs.

  18. USE OF COAL DRYING TO REDUCE WATER CONSUMED IN PULVERIZED COAL POWER PLANTS

    Energy Technology Data Exchange (ETDEWEB)

    Edward Levy

    2005-10-01

    Low rank fuels such as subbituminous coals and lignites contain significant amounts of moisture compared to higher rank coals. Typically, the moisture content of subbituminous coals ranges from 15 to 30 percent, while that for lignites is between 25 and 40 percent, where both are expressed on a wet coal basis. High fuel moisture has several adverse impacts on the operation of a pulverized coal generating unit. High fuel moisture results in fuel handling problems, and it affects heat rate, mass rate (tonnage) of emissions, and the consumption of water needed for evaporative cooling. This project deals with lignite and subbituminous coal-fired pulverized coal power plants, which are cooled by evaporative cooling towers. In particular, the project involves use of power plant waste heat to partially dry the coal before it is fed to the pulverizers. Done in a proper way, coal drying will reduce cooling tower makeup water requirements and also provide heat rate and emissions benefits. The technology addressed in this project makes use of the hot circulating cooling water leaving the condenser to heat the air used for drying the coal (Figure 1). The temperature of the circulating water leaving the condenser is usually about 49 C (120 F), and this can be used to produce an air stream at approximately 43 C (110 F). Figure 2 shows a variation of this approach, in which coal drying would be accomplished by both warm air, passing through the dryer, and a flow of hot circulating cooling water, passing through a heat exchanger located in the dryer. Higher temperature drying can be accomplished if hot flue gas from the boiler or extracted steam from the turbine cycle is used to supplement the thermal energy obtained from the circulating cooling water. Various options such as these are being examined in this investigation. This is the eleventh Quarterly Report for this project. The background and technical justification for the project are described, including potential benefits

  19. Modeling of pulverized coal combustion stabilization by means of plasma torches

    Energy Technology Data Exchange (ETDEWEB)

    Miroslav Sijercic; Srdjan Belosevic; Predrag Stefanovic [VINCA Institute of Nuclear Science, Belgrade (Serbia and Montenegro)

    2005-07-01

    Application of plasma-system for pulverized coal ignition and combustion stabilization in utility boiler furnaces promises to achieve certain savings compared to the use of heavy oil burners. Plasma torches are built in air-coal dust mixture ducts between coal mills and burners. Characteristics of processes in the ducts with plasma-system for pulverized coal combustion stabilization are analyzed in the paper, with respect to the modeling and numerical simulation of mass, momentum and heat transfer in two-phase turbulent gas particle flow. The simulations have been performed for three different geometries of the air-coal dust mixture ducts with plasma torches, for TENT A1 utility boiler and pulverized lignite Kolubara-Field 'D'. Selected results of numerical simulation of processes are presented. The plasma-system thermal effect is discussed regarding corresponding savings of liquid fuel. The results of numerical simulations have been analyzed with respect to the processes in the duct and especially with respect to the influence of the duct shape to a temperature field at the out let cross section, as a basis for the duct geometry optimization. It has been emphasized that numerical simulation of processes can be applied in analysis and optimization of pulverized coal ignition and combustion stabilization and enables efficient and cost-effective scaling-up procedure from laboratory to industrial level. 22 refs., 4 figs.

  20. 燃煤锅炉集成太阳能热发电系统经济性分析%Economic Analysis of the Solar Thermal Power Generation System Integrated With a Pulverized Coal Fired Boiler

    Institute of Scientific and Technical Information of China (English)

    赵军; 杨昆

    2012-01-01

    考虑到系统物质流和能量流的匹配,拟定了2种太阳能与燃煤锅炉集成方案:省煤器前方案和省煤器后方案.基于槽式集热器的热力性能与锅炉的变工况理论建立分析模型.以LS-2槽式集热器与某600 MW亚临界锅炉为例,对2种方案进行模拟,总结了太阳能热与锅炉集成时热经济性变化规律,并据此分析2种方案的经济性,结果表明锅炉集成太阳能发电成本低于单纯太阳能热发电方式(solar energy generating systems,SEGS)成本,考虑碳减排效益后,发电成本将进一步降低;省煤器前方案的太阳能发电成本低于省煤器后方案;锅炉集成太阳能发电成本受设计辐射强度、系统寿命、煤价与碳价、集热器成本的影响.%Two layout schemes, the arrangement before and after economizer, were proposed for the pulverized boiler integrated with solar energy from parabolic trough collectors considering material flows matching energy flows. Based on the thermal performance of parabolic trough collectors and the variant condition computation of boiler, the performance analysis models of two integration arrangements were built. Taking 600 MW subcritical boiler and the LS-2 trough collectors for example, the performance of both schemes were investigated and compared. The thermal economic rules for both integration arrangements were summarized in accordance with the simulation results. The economic analysis of the both integration arrangements show that the solar LEC of both schemes is lower than that of solar energy generating systems (SEGS), and while CO2 avoidance is included, the solar LEC is much lower and that the solar LEC of the arrangement before economizer is lower than that of the arrangement after economizer. The solar LEC of both integration arrangements is influenced by the direct solar irradiance, the economic life of the integration systems, coal and CO2 price, the cost of the trough collector.

  1. New computer program plots coal particle size to monitor pulverizer performance

    Energy Technology Data Exchange (ETDEWEB)

    Tartar, A.M. (Univ. of Missouri, St. Louis, MO (United States)); Mueller, W.K. (Union Electric Co., St. Louis, MO (United States)); Marrero, T.R.

    1994-11-01

    Maintaining proper coal particle size and distribution is one of many considerations in achieving efficient combustion performance. Improper pulverizer operation and maintenance can result in an excessive percentage of either coarse coal particles, which tends to increase the amount of unburned carbon in the ash, or fine coal particles, which can limit the throughput of the pulverizer and, if too fine, can affect coal burning rates and residence time in boilers. Traditionally, coal particle size plotting and distribution have been done by hand and required special graphing paper formulated using the Rosin and Rammler equation. Now there is an alternative. This article describes a computerized procedure for plotting the fineness of coal particles after the milling process developed by engineers at Union Electric Co., St. Louis, Mo., and the University of Missouri, Columbia. Known as an ANTAR-UE, this procedure is being used by the Betterment Engineering group at Union Electric to plot mill fineness data.

  2. Microfine coal firing results from a retrofit gas/oil-designed industrial boiler

    Energy Technology Data Exchange (ETDEWEB)

    Patel, R.; Borio, R.W.; Liljedahl, G. [Combustion Engineering, Inc., Windsor, CT (United States)] [and others

    1995-11-01

    Under US Department of Energy, Pittsburgh Energy Technology Center (PETC) support, the development of a High Efficiency Advanced Coal Combustor (HEACC) has been in progress since 1987 at the ABB Power Plant Laboratories. The initial work on this concept produced an advanced coal firing system that was capable of firing both water-based and dry pulverized coal in an industrial boiler environment.

  3. Flexibility of a 300 MW Arch Firing Boiler Burning Low Quality Coals

    Institute of Scientific and Technical Information of China (English)

    2007-01-01

    Experimental investigations on the flexibility of a 300 MW Arch Firing (AF) coal-fired boiler when burning low quality coals is reported.Measurements of gas temperature and species concentration and char sampling using a water-cooled suction pyrometer were carried out along the furnace elevation.The carbon content and the size distributions of the char samples were obtained.The char morphology was examined using a field emission scanning electron microscope (FESEM).The char sampling was performed on this type of boiler for the first time.The results indicate that the flexibility of this boiler burning low quality coals under a moderate boiler load is better than its flexibility under a high boiler load.Because of the insufficient capacity of the coal pulverizers used, in case of low coal quality the pulverized coal fineness will drastically decrease under high boiler loads.This causes an increase in the loss due to incomplete mechanical and chemical combustion.This is the main cause of a low burnout degree of the pulverized coal and the decrease of the flexibility of this AF boiler under a high boiler load.

  4. CFD analysis of the pulverized coal combustion processes in a 160 MWe tangentially-fired-boiler of a thermal power plant

    OpenAIRE

    Silva,Cristiano V. da; Indrusiak,Maria Luiza S; Beskow,Arthur B

    2010-01-01

    The strategic role of energy and the current concern with greenhouse effects, energetic and exergetic efficiency of fossil fuel combustion greatly enhance the importance of the studies of complex physical and chemical processes occurring inside boilers of thermalpower plants. The state of the art in computational fluid dynamics and the availability of commercial codes encourage numeric studies of the combustion processes. In the presentwork the commercial software CFX © Ansys Europe Ltd. was ...

  5. Stabilization of pulverized coal combustion by plasma assist

    Energy Technology Data Exchange (ETDEWEB)

    Sugimoto, M.; Maruta, K.; Takeda, K.; Solonenko, O.P.; Sakashita, M.; Nakamura, M. [Akita Prefectural University, Akita (Japan). Faculty of System Science & Technology

    2002-03-01

    Ignition and stabilization of pulverized coal combustion by plasma assist is investigated with a 10 kW plasma torch for three different kinds of coal, such as high, medium and low volatile matter coals. Not only high volatile matter coal but also low quality coal can be successfully burned with plasma assist. Research for volatile component of coal shows that a higher temperature field is necessary to extract the volatile matter from inferior coal, while their compositions are almost the same.

  6. Trace element emissions when firing pulverized coal in a pilot-scale combustion facility

    Energy Technology Data Exchange (ETDEWEB)

    Miller, S.F.; Wincek, R.T.; Miller, B.G.; Scaroni, A.W.

    1998-07-01

    Strategies are being developed at Penn State to produce ultralow emissions when firing coal-based fuels, i.e., micronized coal and coal-water slurry fuel (CWSF), in industrial boilers. The work is being conducted on the bench, pilot, and demonstration scale, and the emissions being addressed are SO{sub 2}, NO{sub x}, fine particulate matter (PM{sub 10} and PM{sub 2.5}), and air toxics (trace elements and volatile organic compounds). Technical issues related to trace element emissions that are to be addressed include: (1) the effectiveness of coal cleaning; (2) the effect of fuel form (CWSF and pulverized coal); (3) partitioning between the solid and vapor phases; (4) the effect of boiler size; (5) penetration through particulate control devices; (6) the effect of sootblowing; and (7) mercury speciation. This paper discusses the results of preliminary work to determine trace element emissions when firing a raw and cleaned pulverized coal in a pilot-scale combustor. A companion paper, which follows in the proceedings, gives the results of polynuclear aromatic hydrocarbon (PAH) emissions testing in the pilot-scale combustor and in a small industrial boiler. Results from fine particulate testing is found elsewhere in the proceedings.

  7. Measurement and Control of Coal Pipe Temperature of Coal Mills of PF Boiler

    Directory of Open Access Journals (Sweden)

    Karunamoy Chatterjee

    2016-08-01

    Full Text Available Power plant boiler had no arrangement of measure the coal pipe temperature in a continuous basis, though it is an important parameter for any coal fired large boiler. As pulverized coal flows through the long coal-pipe by the help of flow of hot air as a carrier, coal pipe temperature is only the measurement of the coal flow through the pipe to boiler. Low temperature indicates improper flow of pulverized coal through the pipe. So due to no continuous measurement of these parameters we can’t know about the flow profile of coal through pulveriser outlet pipes. Sometimes the pipe got choked and we were not aware of that for a long time. That caused our equipment loss i.e. we had to stop the pulveriser for a long time for de-choking the large size coal pipe. And indirectly it caused loss of power generation and also affected the economical figure of our power house. So to overcome that kind of losses we have to measure the coal pipe temperature in regular basis.

  8. The Unit Thermal Efifciency Inlfuence for Cold Wind Quantitative Change of Pulverized Coal Perparation System of Supercritical Pressure Boiler%超临界锅炉制粉系统冷风量变化对机组热效率的影响

    Institute of Scientific and Technical Information of China (English)

    彭建良; 翟培强

    2015-01-01

    针对我国超临界锅炉实际热效率难以达到设计要求的问题,本文以一台1900t/h超临界锅炉为例,量化分析了制粉系统冷风量变化对排烟温度及锅炉效率的影响,得到不同冷风量与煤耗的关系,提出了提高锅炉运行效率的有益建议。%For the actual supercritical boiler thermal efifciency in our country, it is dififcult to meet the design requirements of the problem, based on a 1900t/h supercritical boiler as an example, the quantitative analysis of the coal pulverizing system cold wind quantity changes on exhaust temperature and boiler efifciency, the inlfuence of different amount of cold air and the relationship between the coal consumption, improve the boiler efifciency is good suggestion are put forward.

  9. A kinetic model of carbon burnout in pulverized coal combustion

    Energy Technology Data Exchange (ETDEWEB)

    Hurt, R.; Jian-Kuan Sun; Lunden, M. [Brown University, Providence, RI (United States). Division of Engineering

    1998-04-01

    The degree of carbon burnout is an important operating characteristic of full-scale suspension-fired coal combustion systems affecting boiler efficiency, electrostatic precipitator operation and the value of fly ash as a saleable product. Prediction of carbon loss requires special char combustion kinetics valid through the very high conversions targeted in industry (typically {gt} 99.5%), and valid for a wide-range of particle temperature histories occurring in full-scale furnaces. The paper presents high-temperature kinetic data for five coal chars in the form of time-resolved burning profiles that include the late stages of combustion. It then describes the development and validation of the Carbon Burnout Kinetic Model (CBK), a coal-general kinetics package that is specifically designed to predict the total extent of carbon burnout and ultimate fly ash carbon content for prescribed temperature/oxygen histories typical of pulverized coal combustion systems. The model combines the single-film treatment of cha oxidation with quantitative descriptions of thermal annealing, statistical kinetics, statistical densities, and ash inhibition in the late stages of combustion. In agreement with experimental observations, the CBK model predicts (1) low reactivities for unburned carbon residues extracted from commercial ash samples, (2) reactivity loss in the late stages of laboratory combustion, (3) the observed sensitivity of char reactivity to high-temperature heat treatment on second and subsecond time scales, and (4) the global reaction inhibition by mineral matter in the late stages of combustion observed in single-particle imaging studies. The model ascribes these various char deactivation phenomena to the combined effects of thermal annealing, ash inhibition, and the preferential consumption of more reactive particles (statistical kinetics), the relative contributions of which vary greatly with combustion conditions. 39 refs., 4 figs., 4 tabs., 1 app.

  10. Ash formation under pressurized pulverized coal combustion conditions

    Science.gov (United States)

    Davila Latorre, Aura Cecilia

    Coal combustion is a source of inorganic particulate matter (ash), which can deposit in boilers and also be emitted into the atmosphere becoming part of ambient fine particulate matter (PM 2.5). In order to decrease coal combustion emissions per unit of power produced, higher efficiency systems have been proposed, including systems operating at elevated pressures. These new operating conditions will affect pollutant formation mechanisms, particularly those associated with the conversion of mineral matter to ash. Ash particle formation mechanisms are particularly sensitive to changes in pressure as they are related to the structure of coal char particles at early stages of combustion. To assess the importance of pressure on ash particle formation, pyrolyzed chars and ash particles from pressurized pulverized combustion of two bituminous and one subbituminous U.S. coals at operating pressures up to 30 atm were studied. Pressure changes the distribution of char particle types, changing the spatial distribution of the minerals during the combustion process and therefore affecting particle formation mechanisms. Chars were examined by Scanning Electron Microscopy (SEM) and classified into two different types (cenospheric and solid) depending on porosity and wall thickness. A correlation for estimating the amount of these cenospheric char particles was then proposed for bituminous coals based on the operating conditions and coal maceral analysis. The ash particle size distribution of the coals combusted at different operating pressures was measured using Computer Controlled Scanning Electron Microscopy (CCSEM). The results of the char characterization and ash particle size distribution measurements were then incorporated into an ash particle formation algorithm that was proposed and implemented. The model predicts ash particle size and composition distributions at elevated pressures under conditions of complete char burnout. Ash predictions were calculated by first

  11. USE OF COAL DRYING TO REDUCE WATER CONSUMED IN PULVERIZED COAL POWER PLANTS

    Energy Technology Data Exchange (ETDEWEB)

    Edward K. Levy; Nenad Sarunac; Harun Bilirgen; Hugo Caram

    2006-03-01

    U.S. low rank coals contain relatively large amounts of moisture, with the moisture content of subbituminous coals typically ranging from 15 to 30 percent and that for lignites from 25 and 40 percent. High fuel moisture has several adverse impacts on the operation of a pulverized coal generating unit, for it can result in fuel handling problems and it affects heat rate, stack emissions and maintenance costs. Theoretical analyses and coal test burns performed at a lignite fired power plant show that by reducing the fuel moisture, it is possible to improve boiler performance and unit heat rate, reduce emissions and reduce water consumption by the evaporative cooling tower. The economic viability of the approach and the actual impact of the drying system on water consumption, unit heat rate and stack emissions will depend critically on the design and operating conditions of the drying system. The present project evaluated the low temperature drying of high moisture coals using power plant waste heat to provide the energy required for drying. Coal drying studies were performed in a laboratory scale fluidized bed dryer to gather data and develop models on drying kinetics. In addition, analyses were carried out to determine the relative costs and performance impacts (in terms of heat rate, cooling tower water consumption and emissions) of drying along with the development of optimized drying system designs and recommended operating conditions.

  12. 基于流体力学的工业煤粉锅炉配风控制策略%Application of Control Strategy Based on the Fluid Mechanics Principle to the Air Distribution Control of Industry Pulverized Coal Fired Boiler

    Institute of Scientific and Technical Information of China (English)

    麻林

    2014-01-01

    the control strategy is the core of control system, the control strategy can directly influence the in⁃dustrial equipment in operation safety, stable and efficient. The control system is mostly through the feed⁃back signal as a control strategy decision, and the lag of feedback signal, often causes the device to run shocks to adjust time is too long, and even lead to equipment downtime or safety accident. Based on small and medium-sized industrial pulverized coal boiler air distribution control as an example, the application of the air distribution control strategy based on fluid mechanics principle as the foundation, and combining with the feedback signal, effectively reduce boiler shocks to adjust time, make the boiler as soon as possible into the steady combustion state, effectively improve the boiler's safety and stability, further improve the automa⁃tion of industrial coal the boiler level control.%文章以中小型工业煤粉锅炉的配风控制为例,应用了以流体力学原理为基础的配风控制策略,同时结合反馈信号,有效减少锅炉震荡调整时间,使锅炉尽快进入稳定燃烧状态,有效地提高了锅炉的安全性和稳定性,进一步提高工业煤粉锅炉的自动化控制水平。

  13. Temperature, velocity and species profile measurements for reburning in a pulverized, entrained flow, coal combustor

    Energy Technology Data Exchange (ETDEWEB)

    Tree, D.R.

    1999-03-01

    Nitrogen oxide emissions from pulverized coal combustion have been and will continue to be a regulated pollutant for electric utility boilers burning pulverized coal. Full scale combustion models can help in the design of new boilers and boiler retrofits which meet emissions standards, but these models require validation before they can be used with confidence. The objective of this work was to obtain detailed combustion measurements of pulverized coal flames which implement two NO reduction strategies, namely reburning and advanced reburning, to provide data for model validation. The data were also compared to an existing comprehensive pulverized coal combustion model with a reduced mechanism for NO reduction under reburning and advanced reburning conditions. The data were obtained in a 0.2 MW, cylindrical, down-fired, variable swirl, pulverized coal reactor. The reactor had a diameter of 0.76 m and a length of 2.4 m with access ports along the axial length. A Wyodak, sub-bituminous coal was used in all of the measurements. The burner had a centrally located primary fuel and air tube surrounded by heated and variably swirled secondary air. Species of NO, NO{sub x}, CO, CO{sub 2} and O{sub 2} were measured continuously. Aqueous sampling was used to measure HCN and NH{sub 3} at specific reactor locations. Samples were drawn from the reactor using water quenched suction probes. Velocity measurements were obtained using two component laser doppler anemometry in back-scatter mode. Temperature measurements were obtained using a shielded suction pyrometer. A series of six or more radial measurements at six or more axial locations within the reactor provided a map of species, temperature, and velocity measurements. In total, seven reactor maps were obtained. Three maps were obtained at baseline conditions of 0, 0.5 and 1.5 swirl and 10% excess air. Two maps were obtained under reburning conditions of 0.78 stoichiometric ratio and 1.5 swirl and 0.9 stoichiometric ratio and

  14. Experimental study on ignition characteristics of pulverized coal under high-temperature oxygen condition

    Science.gov (United States)

    Liu, G. W.; Liu, Y. H.; Dong, P.

    2016-08-01

    The high-temperature oxygen ignition technology of pulverized coal, which can replace the oil gun and achieve oil-free pulverized coal ignition by mixing the high- temperature oxygen and the pulverized coal stream directly, was proposed and a relevant ignition experimental system was built. The ignition characteristics of pulverized coal under high-temperature oxygen condition were investigated: the ignition process was described and analyzed, the influence of relevant parameters on the pulverized coal stream ignition were obtained and analyzed. The results showed: when the oxygen heating temperature is over 750 °C, the pulverized coal stream could be ignited successfully by high-temperature oxygen; increasing the pulverized coal concentration, primary air temperature and oxygen volume flow rate or decreasing the primary air velocity is helpful for the ignition and combustion of the pulverized coal stream.

  15. Evaluation of dense-phase ultrafine coal (DUC) as a fuel alternative for oil- and gas-designed boilers and heaters. Final report

    Energy Technology Data Exchange (ETDEWEB)

    1986-12-01

    Utility and industrial firms currently using oil- and gas-fired boilers have an interest in substitution of coal for oil and gas as the primary boiler fuel. This interest stems from coal`s two main advantages over oil and gas-lower cost and security of supply. Recent efforts in the area of coal conversion have been directed to converting oil- and gas- fired boilers which were originally designed for coal-firing or were designed with some coal-firing capability. Boilers designed exclusively for oil- or gas-firing have not been considered viable candidates for coal conversion because they generally require a significant capacity derating and extensive and costly modifications. As a result, conversion of boilers in this class to coal-firing has generally been considered unattractive. Renewed interest in the prospects for converting boilers designed exclusively for oil- and gas-firing to coal firing has centered around the concept of using ``ultra fine`` coal as opposed to ``conventional grind`` pulverized coal. The main distinction being the finer particle size to which the former is ground. This fuel type may have characteristics which ameliorate many of the boiler problems normally associated with pulverized coal-firing. The overall concept for ultrafine coal utilization is based on a regional large preparation plant with distribution of a ready to fire fuel directly to many small users. This differs from normal practice in which final coal sizing is performed in pulverizers at the user`s site.

  16. Ash chemistry aspects of straw and coal-straw co-firing in utility boilers

    Energy Technology Data Exchange (ETDEWEB)

    Frandsen, F.; Nielsen, H.P.; Hansen, L.A.; Hansen, P.F.B.; Andersen, K.H.; Soerensen, H.S.

    1998-12-01

    Deposits formed in straw-fired grate-boilers showed significant amounts of KCl ( 40 - 80 % (w/w)) and KCl-coated Ca-Si-rich particles. CFB co-firing of straw and coal caused deposits in the convective pass containing predominantly K{sub 2}SO{sub 4} (50 - 60 % (w/w)) with small amounts of KCl close to the metal surface. In pulverized coal-straw co-fired boilers, deposits almost free of KCl were found. Most of the potassium in these deposits is derived from K-Al-Si-rich fly ash particles and the rest occurs as K{sub 2}SO{sub 4}. The presence of K-Al-Si-rich fly ash particles indicates that solid residue quality and reuse of fly ash in cement and concrete production rather than deposit formation may be of concern when utilizing straw in pulverized fuel boilers. This paper provides a review of Danish experiences with high-temperature ash deposit formation in the following full-scale utility boilers: Slagelse CHP (31 MW{sub th}), Haslev CHP (23 MW{sub th}) and Rudkoebing CHP (10.7 MW{sub th}), all straw-fired grate-boilers; Grenaa CHP (80 MW{sub th}), a coal-straw co-fired Circulating Fluidized Bed (CFB) boiler; and the Midtkraft-Studstrup Power Station, Unit l (380 MW{sub th}), a coal-straw co-fired pf-boiler. (au)

  17. Modelling of coal combustion enhanced through plasma-fuel systems in full-scale boilers

    Energy Technology Data Exchange (ETDEWEB)

    A.S. Askarova; Z. Jankoski; E.I. Karpenko; E.I. Lavrischeva; F.C. Lockwood; V.E. Messerle; A.B. Ustimenko [al-Farabi Kazakh National University, Almaty (Kazakhstan). Department of Physics

    2005-07-01

    Plasma activation promotes more effective and environmental friendly low-rank coal combustion. This work presents numerical modelling results of plasma thermochemical preparation of pulverized coal for ignition and combustion in the furnace of a utility boiler. Two kinetic mathematical models were used in the investigation of the processes of air-fuel mixture plasma activation, ignition and combustion. A 1D kinetic code, PLASMA-COAL, calculates the concentrations of species, temperatures and velocities of treated coal-air mixtures in a burner incorporating a plasma source. It gives initial data for 3D-modeling of power boilers furnaces by the code FLOREAN. A comprehensive image of plasma activated coal combustion processes in a furnace of pulverised coal fired boiler was obtained. The advantages of the plasma technology are clearly demonstrated. 15 refs., 6 figs., 4 tabs.

  18. The demonstration of an advanced cyclone coal combustor, with internal sulfur, nitrogen, and ash control for the conversion of a 23 MMBTU/hour oil fired boiler to pulverized coal

    Energy Technology Data Exchange (ETDEWEB)

    Zauderer, B.; Fleming, E.S.

    1991-08-30

    This work contains to the final report of the demonstration of an advanced cyclone coal combustor. Titles include: Chronological Description of the Clean Coal Project Tests,'' Statistical Analysis of Operating Data for the Coal Tech Combustor,'' Photographic History of the Project,'' Results of Slag Analysis by PA DER Module 1 Procedure,'' Properties of the Coals Limestone Used in the Test Effort,'' Results of the Solid Waste Sampling Performed on the Coal Tech Combustor by an Independent Contractor During the February 1990 Tests.'' (VC)

  19. A new approach to study fast pyrolysis of pulverized coal

    Energy Technology Data Exchange (ETDEWEB)

    Wang, J.; Yao, J.; Lin, W. [Chinese Academy of Sciences, Institute of Chemical Metallurgy Fast Reactions Laboratory, Beijing, BJ (China)

    2002-07-01

    An experimental study of the effects of varying bed temperature and coal particle size on the fast pyrolysis of pulverized coal in a downer reactor is described. A Datong bituminous coal (particle size 0.5 and 0.34 mm) was studied at temperatures ranging from 592{sup o} C to 720{sup o} C. The experiments were conducted in a batch apparatus. An on-line gas analyzer was used to measure carbon dioxide release curves. The experimental data were used to develop a pyrolysis model that quantifies the fast heating of fine coal particles. 14 refs., 4 figs., 2 tabs.

  20. Reconstruction of the aero-mixture channels of the pulverized coal plant of the 100MW power plant unit

    Directory of Open Access Journals (Sweden)

    Ivanovic Vladan B.

    2011-01-01

    Full Text Available After the last revitalization of thermal power block of 100 MW in TPP “Kostolac A”, made in the year 2004, during the operation of the plant, pulverized coal deposition often occurred in horizontal sections of the aero-mixture channels. Deposition phenomenon manifested itself in places ahead of spherical compensators in the direction of flow of pulverized coal to the burners, due to unfavorable configuration of these channels. Coal dust deposited in the channels dried and spontaneously combusted, causing numerous damage to channels and its isolation as well as the frequent stoppage of the operation for necessary interventions. The paper presents the original solution of reconstruction of aero-mixture channels which prevented deposition of coal dust and its eventual ignition. In this way the reliability of the mill plant is maximized and higher availability of boiler and block as a whole is achieved.

  1. Impact of Coal Fly Ash Addition on Combustion Aerosols (PM2.5) from Full-Scale Suspension-Firing of Pulverized Wood

    DEFF Research Database (Denmark)

    Damø, Anne Juul; Wu, Hao; Frandsen, Flemming

    2014-01-01

    The formation of combustion aerosols was studied in an 800 MWth suspension-fired power plant boiler, during combustion of pulverized wood pellets with and without addition of coal fly ash as alkali capture additive. The aerosol particles were sampled and characterized by a low-pressure cascade...

  2. Impact of nongray multiphase radiation in pulverized coal combustion

    Science.gov (United States)

    Roy, Somesh; Wu, Bifen; Modest, Michael; Zhao, Xinyu

    2016-11-01

    Detailed modeling of radiation is important for accurate modeling of pulverized coal combustion. Because of high temperature and optical properties, radiative heat transfer from coal particles is often more dominant than convective heat transfer. In this work a multiphase photon Monte Carlo radiation solver is used to investigate and to quantify the effect of nongray radiation in a laboratory-scale pulverized coal flame. The nongray radiative properties of carrier phase (gas) is modeled using HITEMP database. Three major species - CO, CO2, and H2O - are treated as participating gases. Two optical models are used to evaluate radiative properties of coal particles: a formulation based on the large particle limit and a size-dependent correlation. Effect of scattering due to coal particle is also investigated using both isotropic scattering and anisotropic scattering using a Henyey-Greenstein function. Lastly, since the optical properties of ash is very different from that of coal, the effect of ash content on the radiative properties of coal particle is examined. This work used Extreme Science and Engineering Discovery Environment (XSEDE), which is supported by National Science Foundation Grant Number ACI-1053575.

  3. NITRIC OXIDE FORMATION DURING PULVERIZED COAL COMBUSTION

    Science.gov (United States)

    Data on the overall conversion of coal-nitrogen to NOx were obtained at 1250 K and 1750 K for a residence time of one second. The conversion of coal-nitrogen to NOx decreased monotonically with increasing fuel/oxygen equivalence ratio and decreased slightly with increasing temper...

  4. Modeling of Pulverized Coal Combustion in Cement Rotary Kiln

    OpenAIRE

    2006-01-01

    In this paper, based on analysis of the chemical and physical processes of clinker formation, a heat flux function was introduced to take account of the thermal effect of clinker formation. Combining the models of gas-solid flow, heat and mass transfer, and pulverized coal combustion, a set of mathematical models for a full-scale cement rotary kiln were established. In terms of commercial CFD code (FLUENT), the distributions of gas velocity, gas temperature, and gas components in a cement rot...

  5. NOx CONTROL OPTIONS AND INTEGRATION FOR US COAL FIRED BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    Mike Bockelie; Marc Cremer; Kevin Davis; Connie Senior; Bob Hurt; Eric Eddings; Larry Baxter

    2001-10-10

    This is the fifth Quarterly Technical Report for DOE Cooperative Agreement No: DE-FC26-00NT40753. The goal of the project is to develop cost effective analysis tools and techniques for demonstrating and evaluating low NOx control strategies and their possible impact on boiler performance for firing US coals. The Electric Power Research Institute (EPRI) is providing cofunding for this program. This program contains multiple tasks and good progress is being made on all fronts. Field tests for NOx reduction in a cyclone fired utility boiler due to using Rich Reagent Injection (RRI) have been started. CFD modeling studies have been started to evaluate the use of RRI for NOx reduction in a corner fired utility boiler using pulverized coal. Field tests of a corrosion monitor to measure waterwall wastage in a utility boiler have been completed. Computational studies to evaluate a soot model within a boiler simulation program are continuing. Research to evaluate SCR catalyst performance has started. A literature survey was completed. Experiments have been outlined and two flow reactor systems have been designed and are under construction. Commercial catalyst vendors have been contacted about supplying catalyst samples. Several sets of new experiments have been performed to investigate ammonia removal processes and mechanisms for fly ash. Work has focused on a promising class of processes in which ammonia is destroyed by strong oxidizing agents at ambient temperature during semi-dry processing (the use of moisture amounts less than 5 wt-%). Both ozone and an ozone/peroxide combination have been used to treat both basic and acidic ammonia-laden ashes.

  6. NOx CONTROL OPTIONS AND INTEGRATION FOR US COAL FIRED BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    Mike Bockelie; Marc Cremer; Kevin Davis; Connie Senior; Bob Hurt; Eric Eddings; Larry Baxter

    2001-10-10

    This is the fifth Quarterly Technical Report for DOE Cooperative Agreement No: DE-FC26-00NT40753. The goal of the project is to develop cost effective analysis tools and techniques for demonstrating and evaluating low NOx control strategies and their possible impact on boiler performance for firing US coals. The Electric Power Research Institute (EPRI) is providing cofunding for this program. This program contains multiple tasks and good progress is being made on all fronts. Field tests for NOx reduction in a cyclone fired utility boiler due to using Rich Reagent Injection (RRI) have been started. CFD modeling studies have been started to evaluate the use of RRI for NOx reduction in a corner fired utility boiler using pulverized coal. Field tests of a corrosion monitor to measure waterwall wastage in a utility boiler have been completed. Computational studies to evaluate a soot model within a boiler simulation program are continuing. Research to evaluate SCR catalyst performance has started. A literature survey was completed. Experiments have been outlined and two flow reactor systems have been designed and are under construction. Commercial catalyst vendors have been contacted about supplying catalyst samples. Several sets of new experiments have been performed to investigate ammonia removal processes and mechanisms for fly ash. Work has focused on a promising class of processes in which ammonia is destroyed by strong oxidizing agents at ambient temperature during semi-dry processing (the use of moisture amounts less than 5 wt-%). Both ozone and an ozone/peroxide combination have been used to treat both basic and acidic ammonia-laden ashes.

  7. A simple numerical model to estimate the effect of coal selection on pulverized fuel burnout

    Energy Technology Data Exchange (ETDEWEB)

    Sun, J.K.; Hurt, R.H.; Niksa, S.; Muzio, L.; Mehta, A.; Stallings, J. [Brown University, Providence, RI (USA). Division Engineering

    2003-06-01

    The amount of unburned carbon in ash is an important performance characteristic in commercial boilers fired with pulverized coal. Unburned carbon levels are known to be sensitive to fuel selection, and there is great interest in methods of estimating the burnout propensity of coals based on proximate and ultimate analysis - the only fuel properties readily available to utility practitioners. A simple numerical model is described that is specifically designed to estimate the effects of coal selection on burnout in a way that is useful for commercial coal screening. The model is based on a highly idealized description of the combustion chamber but employs detailed descriptions of the fundamental fuel transformations. The model is validated against data from laboratory and pilot-scale combustors burning a range of international coals, and then against data obtained from full-scale units during periods of coal switching. The validated model form is then used in a series of sensitivity studies to explore the role of various individual fuel properties that influence burnout.

  8. Trace element emissions when firing pulverized coal in a pilot-scale combustion facility

    Energy Technology Data Exchange (ETDEWEB)

    Miller, S.F.; Wincek, R.T.; Miller, B.G.; Scaroni, A.W. [Pennsylvania State Univ., University Park, PA (United States)

    1998-04-01

    Title Ed of the Clean Air Act Amendments of 1990 designates 189 hazardous air pollutants (HAPs). Fourteen of the 189 substances identified are: antimony (Sb), beryllium (Be), chlorine (0), cobalt (Co), manganese (Mn), nickel (Ni), selenium (Se), fluorine (F), arsenic (As), cadmium (Cd), chromium (Cr), lead (Pb), mercury (Hg), and phosphorous (P). Eleven of these elements have been detected in the flue gas of pulverized coal-fired utility boilers. Currently there are no regulations that limit the emissions of these elements during coal combustion in utility- or industrial-scale boilers. Given the growing body of risk assessment data on these elements and their impact on the environment and human health, it is possible that regulations on emission levels for certain elements will be imposed. A knowledge of the occurrence of trace elements in coal and their behavior during combustion is essential to predict emissions and to develop control technologies for remediation. The partitioning of trace elements during combustion can be traced to their volatility within the system. For purposes of this paper, the classification of trace elements summarized by Clarke and Sloss will be used: Group I elements, i.e., elements that are not easily volatilized and form larger bottom ash and fly ash particles; Group H elements, i.e., elements that are partially or completely volatilization followed by condensation as small particles or on the surface of small particles; and Group III elements, i.e., elements that are readily volatilized and usually remain in the gas phase system.

  9. Boiler derating for coal-water mixtures

    Energy Technology Data Exchange (ETDEWEB)

    Horney, F.A.; Nolte, F.S.

    1983-11-01

    The authors demonstrated a method for approximating the derating required when converting an oil or natural gas fired unit to a coal-water mixture. If the results show that a retrofit to coal-water mixture appears economically reasonable, then a more detailed analysis should be made by the boiler manufacturer whose methods are more precise than the methods of this paper. The expense of having the boiler manufacturer make a precise analysis can be avoided if the results of the analysis of this paper show conversion not to be viable.

  10. Application of BCS technology in pulverized coal furnace%BCS技术在煤粉炉上的应用

    Institute of Scientific and Technical Information of China (English)

    高瑞峰; 于现军

    2015-01-01

    BCS是应用于燃烧过程的通用优化控制技术,已成功应用于链条炉、 CFB锅炉、高炉热风炉、轧钢加热炉等多种炉型。在此基础上, BCS首次在某热电厂3台65 t/h煤粉炉上得到应用,并取得了良好的运行效果。%BCS is a sort of general optimization control technology for combustion process, which has been successfully applied to CFB boiler , chain boiler, hot stove for blast furnace, and reheating fur-nace for rolling etc.The optimization control system based on BCS was first put into use for 3 ×65t/h pulverized coal boiler and gets good results.

  11. Experimental study on the angle of repose of pulverized coal

    Institute of Scientific and Technical Information of China (English)

    Wei Wang; Jiansheng Zhang; Shi Yang; Hai Zhang; Hairui Yang; Guangxi Yue

    2010-01-01

    An experimental study on the angle of repose(AoR)of pulverized coal with different particle sizes and different moisture contents(MC)was conducted.Three different measurement methods,free-base piling,fixed-base piling and sliding,were used.The data were analyzed by one-way and two-way analysis of variance.The results showed that the AoRs of pulverized coal with particle sizes smaller than 150 μm were in the range of 30-50°.The characterization of the flowability of pulverized coal was some cohesiveness or true cohesiveness.The increase of MC will increase AoR and thus decrease the flowability of the powder.However,the particle size effect is bifurcated.Below a critical size,the decrease of particle size decreases the flowability; while above the critical size,the decrease of particle size increases the flowability.It was found that the value of the critical size strongly depends on the powder density.Moreover,the AoR dependence on particle size could be linked with the Geldart's particle classification.The critical size at the turning point is on the boundary between Group A and Group B in Geldart's classification diagram.Based on the experimental results,there is no significant cross interaction between particle size and MC.The AoRs measured by free-base method and fixed-base method are close,but both remarkably smaller than that measured by the sliding method.

  12. BOILER MATERIALS FOR ULTRASUPERCRITICAL COAL POWER PLANTS

    Energy Technology Data Exchange (ETDEWEB)

    R. Viswanathan; K. Coleman; R.W. Swindeman; J. Sarver; J. Blough; W. Mohn; M. Borden; S. Goodstine; I. Perrin

    2003-10-20

    The principal objective of this project is to develop materials technology for use in ultrasupercritical (USC) plant boilers capable of operating with 760 C (1400 F), 35 MPa (5000 psi) steam. This project has established a government/industry consortium to undertake a five-year effort to evaluate and develop of advanced materials that allow the use of advanced steam cycles in coal-based power plants. These advanced cycles, with steam temperatures up to 760 C, will increase the efficiency of coal-fired boilers from an average of 35% efficiency (current domestic fleet) to 47% (HHV). This efficiency increase will enable coal-fired power plants to generate electricity at competitive rates (irrespective of fuel costs) while reducing CO{sub 2} and other fuel-related emissions by as much as 29%. Success in achieving these objectives will support a number of broader goals. First, from a national prospective, the program will identify advanced materials that will make it possible to maintain a cost-competitive, environmentally acceptable coal-based electric generation option. High sulfur coals will specifically benefit in this respect by having these advanced materials evaluated in high-sulfur coal firing conditions and from the significant reductions in waste generation inherent in the increased operational efficiency. Second, from a national prospective, the results of this program will enable domestic boiler manufacturers to successfully compete in world markets for building high-efficiency coal-fired power plants.

  13. Numerical simulation of the influence of stationary louver and coal particle size on distribution of pulverized coal to the feed ducts of a power plant burner

    Directory of Open Access Journals (Sweden)

    Živković Goran

    2009-01-01

    Full Text Available One of the key requirements related to successful utilization of plasma technology as an oil-free backup system for coal ignition and combustion stabilization in power plant boilers is provision of properly regulated pulverized coal distribution to the feed ducts leading the fuel mixture to a burner. Proper regulation of coal distribution is deemed essential for achieving an adequate pulverized coal concentration in the zone where thermal plasma is being introduced. The said can be efficiently achieved by installation of stationary louver in the coal-air mixing duct ahead of the feed ducts of a burner. The paper addresses numerical simulation of a two-phase flow of air-pulverized coal mixture in the mixing ducts, analyzing the effects of particle size distribution on pulverized coal distribution to the burner feed ducts. Numerical simulation was performed using the FLUENT 6.3 commercial code and related poly-dispersed flow module, based on the PSI-CELL approach. Numerical experiments have been performed assuming a mono-dispersed solid phase with particle diameter ranging from 45 mm to 1200 mm. Distance between the louver blades and the resulting effect on the flow profile was analyzed as well. Results obtained indicate that the size of coal particles considerably influence the overall solid phase distribution. While fine particles, with diameters at the lower end of the above specified range, almost fully follow the streamlines of the continuous phase, coarser particles, which hit the louver blades, deflect towards the thermal plasma zone. In this manner, a desired phase concentration in the considered zone can be reached. For the said reason, installation of stationary louver have been deemed a very efficient way to induce phase separation, primarily due to more pronounced impact of the installed louver on discrete phase flow then the impact on the flow of the continuous phase.

  14. Demonstration of coal reburning for cyclone boiler NO{sub x} control. Appendix, Book 1

    Energy Technology Data Exchange (ETDEWEB)

    1994-06-01

    Based on the industry need for a pilot-scale cyclone boiler simulator, Babcock Wilcox (B&W) designed, fabricated, and installed such a facility at its Alliance Research Center (ARC) in 1985. The project involved conversion of an existing pulverized coal-fired facility to be cyclone-firing capable. Additionally, convective section tube banks were installed in the upper furnace in order to simulate a typical boiler convection pass. The small boiler simulator (SBS) is designed to simulate most fireside aspects of full-size utility boilers such as combustion and flue gas emissions characteristics, fireside deposition, etc. Prior to the design of the pilot-scale cyclone boiler simulator, the various cyclone boiler types were reviewed in order to identify the inherent cyclone boiler design characteristics which are applicable to the majority of these boilers. The cyclone boiler characteristics that were reviewed include NO{sub x} emissions, furnace exit gas temperature (FEGT) carbon loss, and total furnace residence time. Previous pilot-scale cyclone-fired furnace experience identified the following concerns: (1) Operability of a small cyclone furnace (e.g., continuous slag tapping capability). (2) The optimum cyclone(s) configuration for the pilot-scale unit. (3) Compatibility of NO{sub x} levels, carbon burnout, cyclone ash carryover to the convection pass, cyclone temperature, furnace residence time, and FEGT.

  15. An investigation on polycyclic aromatic hydrocarbon emissions from pulverized coal combustion systems

    Science.gov (United States)

    Pisupati; Wasco; Scaroni

    2000-05-29

    Results from a series of tests conducted to study the emission of polynuclear or polycyclic aromatic hydrocarbons (PAHs) from bench-scale and small industrial, water-tube boiler are discussed. A Middle Kittanning, and Upper Freeport seam coals were used in the study. Samples were extracted from the reactor outlet and from the inlet and outlet sides of the research boiler's (RB) baghouse using EPA promulgated methods.Only acenaphthene and fluoranthene were detected in down-fired combustor (DFC) samples. In addition to these two, naphthalene was detected in the RB samples. Emission factors ranged from 80 to 320 &mgr;g/kg of fuel fired. Although there were minor trends in the emissions' data, given the reproducibility limits for PAH compounds, no significant differences were found in the emissions with respect to the fuel type or form (pulverized coal (PC) vs. coal-water slurry fuel (CWSF), and raw vs. cleaned coal) and firing conditions (high and low excess air). The PAH emissions showed a decrease with increase in the firing rate.A bench-scale drop-tube reactor (DTR) was used to study the effects of temperature and residence time on PAH formation. The results revealed near constant PAH concentrations in the solid-phase samples, while the PAH concentrations in the vapor-phase samples increased as a function of temperature. At a temperature of around 1300 degrees C, the rate of PAH formation was exceeded by the rate of PAH oxidation, and PAH concentrations in the vapor phase began to decrease.

  16. Technical improvement on the volume of desuperheating water in pulverized coal fired boiler%降低煤粉锅炉减温水量的技术改造

    Institute of Scientific and Technical Information of China (English)

    施万森

    2012-01-01

    Aiming at the temperature of the superheater and reheater was higher, the volume of desuperheating water was large and safe stability of the boiler was poor, in two boilers of a power genera- tion company, through improving the heating surface of boiler afterbody, increases heat absorption capacity of heating surface of economizer, reduces heat absorption capacity of superheater and reheater, reaches the aim of reducing the volume of desuperheating water. The result shows that the volume of desuperheating water is 100t/h after the improvement, reduces greatly than formerly, promotes safe stability and economy of the boiler' s oneration.%针对某发电公司2台锅炉存在过热器和再热汽温偏高、减温水量大、锅炉安全稳定性差的问题,通过对锅炉尾部受热面进行改造,增加省煤器受热面的吸热量,减少了过热器、再热器的吸热量,达到了降低减温水量的目的。改造结果表明:减温水量减少到100t/h,比改造前大大降低,提高了锅炉运行的安全稳定性及经济性。

  17. COAL COMBUSTION EFFICIENCY IN CFB BOILER

    Institute of Scientific and Technical Information of China (English)

    Hairui Yang; Guangxi Yue

    2005-01-01

    The carbon content in the fly ash from most Chinese circulating fluidized bed (CFB) boilers is much higher than expected, thus directly influencing the combustion efficiency. In the present paper, carbon burnout was investigated both in field tests and laboratory experiments. The effect of coal property, operation condition, gas-solid mixing, char deactivation,residence time and cyclone performance are analyzed seriatim based on large amount of experimental results.A coal index is proposed to describe the coal rank, defined by the ratio of the volatile content to the coal heat value, is a useful parameter to analyze the char burnout. The carbon content in the fly ash depends on the coal rank strongly. CFB boilers burning anthracite, which has low coal index, usually have high carbon content in the fly ash. On the contrary, the CFB boilers burning brown coal, which has high coal index, normally have low carbon content.Poor gas-solid mixing in the furnace is another important reason of the higher carbon content in the fly ash. Increasing the velocity and rigidity of the secondary air could extend the penetration depth and induce more oxygen into the furnace center. Better gas solid mixing will decrease the lean oxygen core area and increase char combustion efficiency.The fine char particles could be divided into two groups according to their reactivity. One group is "fresh" char particles with high reactivity and certain amount of volatile content. The other group of char particles has experienced sufficient combustion time both in the furnace and in the cyclone, with nearly no volatile. These "old" chars in the fly ash will be deactivated during combustion of large coal particles and have very low carbon reactivity. The generated fine inert char particles by attrition of large coal particles could not easily burn out even with the fly ash recirculation. The fraction of large coal particles in coal feed should be reduced during fuel preparation process.The cyclone

  18. BOILER MATERIALS FOR ULTRASUPERCRITICAL COAL POWER PLANTS

    Energy Technology Data Exchange (ETDEWEB)

    R. Viswanathan; K. Coleman

    2002-10-15

    The principal objective of this project is to develop materials technology for use in ultrasupercritical (USC) plant boilers capable of operating with 760 C (1400 F), 35 MPa (5000 psi) steam. In the 21st century, the world faces the critical challenge of providing abundant, cheap electricity to meet the needs of a growing global population while at the same time preserving environmental values. Most studies of this issue conclude that a robust portfolio of generation technologies and fuels should be developed to assure that the United States will have adequate electricity supplies in a variety of possible future scenarios. The use of coal for electricity generation poses a unique set of challenges. On the one hand, coal is plentiful and available at low cost in much of the world, notably in the U.S., China, and India. Countries with large coal reserves will want to develop them to foster economic growth and energy security. On the other hand, traditional methods of coal combustion emit pollutants and CO{sub 2} at high levels relative to other generation options. Maintaining coal as a generation option in the 21st century will require methods for addressing these environmental issues. This project has established a government/industry consortium to undertake a five-year effort to evaluate and develop of advanced materials that allow the use of advanced steam cycles in coal-based power plants. These advanced cycles, with steam temperatures up to 760 C, will increase the efficiency of coal-fired boilers from an average of 35% efficiency (current domestic fleet) to 47% (HHV). This efficiency increase will enable coal-fired power plants to generate electricity at competitive rates (irrespective of fuel costs) while reducing CO{sub 2} and other fuel-related emissions by as much as 29%. Success in achieving these objectives will support a number of broader goals. First, from a national prospective, the program will identify advanced materials that will make it possible to

  19. BOILER MATERIALS FOR ULTRASUPERCRITICAL COAL POWER PLANTS

    Energy Technology Data Exchange (ETDEWEB)

    R. Viswanathan; K. Coleman

    2003-01-20

    The principal objective of this project is to develop materials technology for use in ultrasupercritical (USC) plant boilers capable of operating with 760 C (1400 F), 35 MPa (5000 psi) steam. In the 21st century, the world faces the critical challenge of providing abundant, cheap electricity to meet the needs of a growing global population while at the same time preserving environmental values. Most studies of this issue conclude that a robust portfolio of generation technologies and fuels should be developed to assure that the United States will have adequate electricity supplies in a variety of possible future scenarios. The use of coal for electricity generation poses a unique set of challenges. On the one hand, coal is plentiful and available at low cost in much of the world, notably in the U.S., China, and India. Countries with large coal reserves will want to develop them to foster economic growth and energy security. On the other hand, traditional methods of coal combustion emit pollutants and CO{sub 2} at high levels relative to other generation options. Maintaining coal as a generation option in the 21st century will require methods for addressing these environmental issues. This project has established a government/industry consortium to undertake a five-year effort to evaluate and develop of advanced materials that allow the use of advanced steam cycles in coal-based power plants. These advanced cycles, with steam temperatures up to 760 C, will increase the efficiency of coal-fired boilers from an average of 35% efficiency (current domestic fleet) to 47% (HHV). This efficiency increase will enable coal-fired power plants to generate electricity at competitive rates (irrespective of fuel costs) while reducing CO{sub 2} and other fuel-related emissions by as much as 29%. Success in achieving these objectives will support a number of broader goals. First, from a national prospective, the program will identify advanced materials that will make it possible to

  20. BOILER MATERIALS FOR ULTRASUPERCRITICAL COAL POWER PLANTS

    Energy Technology Data Exchange (ETDEWEB)

    R. Viswanathan

    2002-04-15

    The principal objective of this project is to develop materials technology for use in ultrasupercritical (USC) plant boilers capable of operating with 760 C (1400 F), and up to 5500 psi with emphasis upon 35 MPa (5000 psi) steam. In the 21st century, the world faces the critical challenge of providing abundant, cheap electricity to meet the needs of a growing global population while at the same time preserving environmental values. Most studies of this issue conclude that a robust portfolio of generation technologies and fuels should be developed to assure that the United States will have adequate electricity supplies in a variety of possible future scenarios. The use of coal for electricity generation poses a unique set of challenges. On the one hand, coal is plentiful and available at low cost in much of the world, notably in the U.S., China, and India. Countries with large coal reserves will want to develop them to foster economic growth and energy security. On the other hand, traditional methods of coal combustion emit pollutants and CO{sub 2} at high levels relative to other generation options. Maintaining coal as a generation option in the 21st century will require methods for addressing these environmental issues. This project has established a government/industry consortium to undertake a five-year effort to evaluate and develop advanced materials that allow the use of advanced steam cycles in coal-based power plants. These advanced cycles, with steam temperatures up to 760 C, will increase the efficiency of coal-fired boilers from an average of 35% efficiency (current domestic fleet) to 47% (HHV). This efficiency increase will enable coal-fired power plants to generate electricity at competitive rates (irrespective of fuel costs) while reducing CO{sub 2} and other fuel-related emissions by as much as 29%. Success in achieving these objectives will support a number of broader goals. First, from a national prospective, the program will identify advanced

  1. Liquefaction behavior of finely pulverized coal. Chobifunsaitan no ekika hanno kyodo

    Energy Technology Data Exchange (ETDEWEB)

    Sato, Y.; Kamo, T.; Miki, K.; Yamamoto, Y. (National Institute for Resources and Environment, Tsukuba (Japan))

    1992-11-05

    The reaction process of coal liquefaction which uses ultrafine pulverized coal having a particle diameter of several micrometers was investigated in order to improve the catalytic efficiency between coal and catalyst. Two kinds of samples were prepared by crushing Taiheiyo-coal into less than 100-mesh by usual technique and further pulverizing the crushed coal to several [mu]m. When iron oxide catalyst, sulfur and tetralin solvent were used, pulverizing does not bring a significant improvement in conversion rate and the yield of liquefaction oil capable of being distillated. This is considered to be due to the coagulation between fine particles before or during reaction, suggesting the importance of selecting reaction conditions etc. In the case of pulverized coal, hydrogen consumption is high and hydrogenation of heavy fractions such as SRC proceeds. When liquefaction-oil circulating solvent and red mud-sulfur-based catalyst were used, gas yield was low in pulverized coal, but no significant improvement was not shown in oil yield of liquefaction oil. The conversion rate and SRC yield were somewhat high in the case of pulverized coal. 3 figs., 2 tabs.

  2. Boiler startup under conditions of convective heating of the highly reactive coal dust

    Science.gov (United States)

    Zhuikov, A. V.; Kulagin, V. A.; Baranova, M. P.; Glushkov, D. O.

    2016-12-01

    Experimental research of conditions and characteristics of ignition of the pulverized coal (with a particle size of approximately 80 μm) of different-type brown coals (1B, 2B, and 3B) during convective heating by a heated airflow (at a temperature of 425-600°C and velocity of 1-5 m/s) is carried out. The use of low-inertia thermocouples, a high-speed video camera, and dedicated software has made it possible to determine the minimum oxidizer parameters needed for coal dust ignition, and the approximation dependences of a main characteristic of the process under study―ignition delay time―on the air temperature. Results of experimental studies provide a basis for developing an optimal scheme of the boiler startup without heavy oil, which differs from the known schemes by the relatively low energy consumption for fuel-burning initiation. By example of the BKZ 75-39FB boiler, the economic usefulness of applying the boiler startup without heavy oil is shown. This scheme can be implemented using the proposed ignition burner that functions as a part of the direct system of pulverized-fuel preparation.

  3. Optimised control of coal-fired boilers

    Energy Technology Data Exchange (ETDEWEB)

    Owens, D.H.; MacConnell, P.F.A.; Neuffer, D.; Dando, R. [University of Exeter, Exeter (United Kingdom). Centre for System and Control Engineering

    1997-07-01

    The objective of the project is to develop and specify a control methodology that will enable existing coal combustion plant to take maximum advantage of modern control techniques. The research is specifically aimed at chain-grate stoker plant (such as the test facility at the Coal Research Establishment, Cheltenham) on which little work has been done for thirty years yet which still represents a large proportion of industrial coal-fired plant in operation worldwide. In detail, the project: reviewed existing control strategies for moving grate stokers, highlighting their limitations and areas for improvements; carried out plant trials to identify the system characteristics such as response time and input/output behaviour; developed a theoretical process based on physical and chemical laws and backed up by trial data; specified control strategies for a single boiler; simulated and evaluated the control strategies using model simulations; developed of an optimised. Control strategy for a single boiler; and assessed the applicability and effects of this control strategy on multiple boiler installations. 67 refs., 34 figs.

  4. Microfine coal firing results from a retrofit gas/oil-designed industrial boiler

    Energy Technology Data Exchange (ETDEWEB)

    Patel, R.; Borio, R.W.; Liljedahl, G. [Combustion Engineering, Inc., Windsor, CT (United States). ABB Power Plant Labs.; Miller, B.G.; Scaroni, A.W. [Pennsylvania State Univ., University Park, PA (United States). Energy and Fuels Research Center; McGowan, J.G. [Univ. of Massachusetts, Amherst, MA (United States)

    1995-12-31

    The development of a High Efficiency Advanced Coal Combustor (HEACC) has been in progress since 1987 and the ABB Power Plant Laboratories. The initial work on this concept produced an advanced coal firing system that was capable of firing both water-based and dry pulverized coal in an industrial boiler environment. Economics may one day dictate that it makes sense to replace oil or natural gas with coal in boilers that were originally designed to burn these fuels. The objective of the current program is to demonstrate the technical and economic feasibility of retrofitting a gas/oil designed boiler to burn micronized coal. In support of this overall objective, the following specific areas were targeted: A coal handling/preparation system that can meet the technical requirements for retrofitting microfine coal on a boiler designed for burning oil or natural gas; Maintaining boiler thermal performance in accordance with specifications when burning oil or natural gas; Maintaining NOx emissions at or below 0.6 lb/MBtu; Achieving combustion efficiencies of 98% or higher; and Calculating economic payback periods as a function of key variables. The overall program has consisted of five major tasks: (1) A review of current state-of-the-art coal firing system components; (2) Design and experimental testing of a prototype HEACC burner; (3) Installation and testing of a HEACC system in a commercial retrofit application; (4) Economic evaluation of the HEACC concept for retrofit applications; and (5) Long term demonstration under commercial user demand conditions. This paper will summarize the latest key experimental results (Task 3) and the economic evaluation (Task 4) of the HEACC concept for retrofit applications. 28 figs., 6 tabs.

  5. Fluidized coal combustion

    Science.gov (United States)

    Moynihan, P. I.; Young, D. L.

    1979-01-01

    Fluidized-bed coal combustion process, in which pulverized coal and limestone are burned in presence of forced air, may lead to efficient, reliable boilers with low sulfur dioxide and nitrogen dioxide emissions.

  6. Measurement of O2 in the Combustion Chamber of Apulverized Coal Boiler

    Directory of Open Access Journals (Sweden)

    Břetislav Janeba

    2012-01-01

    Full Text Available Operational measurements of the O2 concentration in the combustion chamber of a pulverized coal boiler are not yet common practice. Operators are generally satisfied with measuring the O2 concentration in the second pass of the boiler, usually behind the economizer, where a flue gas sample is extracted for analysis in a classical analyzer. A disadvantage of this approach is that there is a very weak relation between the measured value and the condition in specific locations in the fireplace, e.g. the function of the individual burners and the combustion process as a whole. A new extractionline was developed for measuring the O2 concentration in the combustion chamber. A planar lambda probe is used in this approach. The extraction line is designed to get outputs that can be used directly for diagnosis or management of the combustion in the boiler.

  7. Current and advanced NO/sub x/-control technology for coal-fired industrial boilers

    Energy Technology Data Exchange (ETDEWEB)

    1978-12-01

    A NOx-control-technology assessment study of coal-fired industrial boilers was conducted to examine the effectiveness of combustion-modification methods, including low excess air, staged combustion, and burner modifications. Boiler types considered included overfed and underfed stokers, spreader stokers, pulverized-coal and coal-fired cyclone units. Significant variations in NOx emissions occur with boiler type, firing method, and coal type; a relative comparison of emission-control performance, cost, and operational considerations is presented for each method. Baseline (as-found) emissions from grate-fired stokers were shown to be in the range of 200 to 300 ppM. Similarly, as-found emissions from suspension-fired units were quite low (350 to 600 ppM) as compared to comparably designed utility-sized units. Low excess air was shown to be the most effective method on existing units, reducing emissions by approximately 10%. Evaluation of staged combustion and burner modification, however, were limited due to current boiler designs. Major hardware modification/design and implementation are necessary before the potential of these techniques can be fully evaluated. The study emphasized the numerous operational factors that are of major importance to the user in selecting and implementing a combustion-modification program, including energy considerations, incremental capital and operating costs, corrosion, secondary pollutants, and retrofit potential.

  8. ULTRA LOW NOx INTEGRATED SYSTEM FOR NOx EMISSION CONTROL FROM COAL-FIRED BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    Galen H. Richards; Charles Q. Maney; Richard W. Borio; Robert D. Lewis

    2002-12-30

    ALSTOM Power Inc.'s Power Plant Laboratories, working in concert with ALSTOM Power's Performance Projects Group, has teamed with the U.S. Department of Energy's National Energy Technology Laboratory (DOE NETL) to conduct a comprehensive study to develop/evaluate low-cost, efficient NOx control technologies for retrofit to pulverized coal fired utility boilers. The objective of this project was to develop retrofit NOx control technology to achieve less than 0.15 lb/MMBtu NOx (for bituminous coals) and 0.10 lb/MMBtu NOx (for subbituminous coals) from existing pulverized coal fired utility boilers at a cost which is at least 25% less than SCR technology. Efficient control of NOx is seen as an important, enabling step in keeping coal as a viable part of the national energy mix in this century, and beyond. Presently 57% of U.S. electrical generation is coal based, and the Energy Information Agency projects that coal will maintain a lead in U.S. power generation over all other fuel sources for decades (EIA 1998 Energy Forecast). Yet, coal-based power is being strongly challenged by society's ever-increasing desire for an improved environment and the resultant improvement in health and safety. The needs of the electric-utility industry are to improve environmental performance, while simultaneously improving overall plant economics. This means that emissions control technology is needed with very low capital and operating costs. This project has responded to the industry's need for low NOx emissions by evaluating ideas that can be adapted to present pulverized coal fired systems, be they conventional or low NOx firing systems. The TFS 2000{trademark} firing system has been the ALSTOM Power Inc. commercial offering producing the lowest NOx emission levels. In this project, the TFS 2000{trademark} firing system served as a basis for comparison to other low NOx systems evaluated and was the foundation upon which refinements were made to further

  9. Application of Steam Soot Blower in the Water Cooled Walls of Pulverized Coal Boiler%蒸汽吹灰装置在煤粉锅炉水冷壁上的应用

    Institute of Scientific and Technical Information of China (English)

    赵华; 王菲

    2015-01-01

    主要介绍了马钢220 t/h锅炉蒸汽吹灰系统的设备特性及运行情况,分析了蒸汽吹灰器在运行中存在的问题以及解决措施,估算了蒸汽吹灰所带来的经济效益。%The equipment characteristics and operation state of the steam soot blowing system at the 220 t/h boiler of MaSteel are mainly introduced, problems in operation of the steam soot blower and solutions are analyzed and the economic benefit brought by the steam soot blowing is also estimated.

  10. A study of LNCFS III coal burners on boiler waterwall tube wastage

    Energy Technology Data Exchange (ETDEWEB)

    Abbott, R.C.; Gordon, C.M.; Saunders, M.M.; Bray, A.J. [New York State Electric Gas, Bingamton, NY (United States)

    1996-07-01

    Ultrasonic Testing (UT) of waterwall tubing of a tangentially-fired, sub-critical boiler at Milliken Station of New York State Electric and Gas (NYSEG) was undertaken to determine the effects of the newly installed low NO{sub x} firing system on waterwall tube wastage. During a 1993 outage, the pulverized coal-fired boiler was equipped with an ABB CE Low NO, Concentric Firing System (LNCFS) of the third generation (III) including Staged Overfire Air (SOFA) and a coal pulverizing system capable of improving mill fineness by approximately 30 percent. The study was in conjunction with a Department of Energy Clean Coal Demonstration Project. Three separate thickness, surveys were compared using the Electric Power Research Institute`s (EPRI) Boiler Maintenance Workstation (BMW). The Tube Condition Module of BMW compared a total of 20,556 test locations of the three surveys. The evaluations of the surveys indicate that the short-term effect of low NO{sub x} firing with LNCFS III and increased fineness has moderately reduced the remaining life of the carbon steel boiler tubing in selected locations of the waterfall. Approximately 5 percent of the test locations are experiencing an annual tube wastage of 0.008 inches or greater. Additional testing and analyses are recommended to better understand the longer term effects of the low NO{sub x} firing system and the wastage of selected tubing The influence of boiler operating parameters, such as cyclic duty, proportioning of secondary air, or fuel changes, on waterwall tube wastage should also be evaluated over a longer operating period.

  11. Burnout of pulverized biomass particles in large scale boiler – Single particle model approach

    DEFF Research Database (Denmark)

    Saastamoinen, Jaakko; Aho, Martti; Moilanen, Antero

    2010-01-01

    the particle combustion model is coupled with one-dimensional equation of motion of the particle, is applied for the calculation of the burnout in the boiler. The particle size of biomass can be much larger than that of coal to reach complete burnout due to lower density and greater reactivity. The burner...... location and the trajectories of the particles might be optimised to maximise the residence time and burnout....

  12. Impact of coal fly ash addition on ash transformation and deposition in a full-scale wood suspension-firing boiler

    DEFF Research Database (Denmark)

    Wu, Hao; Bashir, Muhammad Shafique; Jensen, Peter Arendt;

    2013-01-01

    Ash transformation and deposition during pulverized wood combustion in a full-scale power plant boiler of 800 MWth were studied with and without the addition of coal fly ash. The transient ash deposition behavior was characterized by using an advanced deposit probe system at two boiler locations...... constant after a few hours. The formed deposits, especially those at the location with low flue gas temperatures, contained a considerable amount of K2SO4, KCl, and KOH/K2CO3. With the addition of a large amount (about 4 times of the mass flow of wood ash) of coal fly ash to the boiler, these alkali...

  13. Pretreatment of biomass by torrefaction and carbonization for coal blend used in pulverized coal injection.

    Science.gov (United States)

    Du, Shan-Wen; Chen, Wei-Hsin; Lucas, John A

    2014-06-01

    To evaluate the utility potential of pretreated biomass in blast furnaces, the fuel properties, including fuel ratio, ignition temperature, and burnout, of bamboo, oil palm, rice husk, sugarcane bagasse, and Madagascar almond undergoing torrefaction and carbonization in a rotary furnace are analyzed and compared to those of a high-volatile coal and a low-volatile one used in pulverized coal injection (PCI). The energy densities of bamboo and Madagascar almond are improved drastically from carbonization, whereas the increase in the calorific value of rice husk from the pretreatment is not obvious. Intensifying pretreatment extent significantly increases the fuel ratio and ignition temperature of biomass, but decreases burnout. The fuel properties of pretreated biomass materials are superior to those of the low-volatile coal. For biomass torrefied at 300°C or carbonized at temperatures below 500°C, the pretreated biomass can be blended with coals for PCI.

  14. Pulverized coal torch combustion in a furnace with plasma-coal system

    Science.gov (United States)

    Messerle, V. E.; Ustimenko, A. B.; Askarova, A. S.; Nagibin, A. O.

    2010-09-01

    Combustion of a pulverized coal torch has been numerically simulated on the basis of the equations of multicomponent turbulent two-phase flows. The results of three-dimensional simulation of conventional and plasma activated coal combustion in a furnace are presented. Computer code Cinar ICE was verified at coal combustion in the experimental furnace with thermal power of 3 MW that was equipped with plasma-fuel system. Operation of the furnace has been studied at the conventional combustion mode and with plasma activation of coal combustion. Influence of plasma activation of combustion on thermotechnical characteristics of the torch and decrease of carbon loss and nitrogen oxides concentration at the furnace outlet has been revealed.

  15. Detailed model for practical pulverized coal furnaces and gasifiers

    Energy Technology Data Exchange (ETDEWEB)

    Philips, S.D.; Smoot, L.D.

    1989-08-01

    The need to improve efficiency and reduce pollutant emissions commercial furnaces has prompted energy companies to search for optimized operating conditions and improved designs in their fossil-fuel burning facilities. Historically, companies have relied on the use of empirical correlations and pilot-plant data to make decisions about operating conditions and design changes. The high cost of collecting data makes obtaining large amounts of data infeasible. The main objective of the data book is to provide a single source of detailed three-dimensional combustion and combustion-related data suitable for comprehensive combustion model evaluation. Five tasks were identified as requirements to achieve the main objective. First, identify the types of data needed to evaluate comprehensive combustion models, and establish criteria for selecting the data. Second, identify and document available three-dimensional combustion data related to pulverized coal combustion. Third, collect and evaluate three-dimensional data cases, and select suitable cases based on selection criteria. Fourth, organize the data sets into an easy-to-use format. Fifth, evaluate and interpret the nature and quality of the data base. 39 refs., 15 figs., 14 tabs.

  16. Small scale experiment on the plasma assisted thermal chemical preparation and combustion of pulverized coal

    Energy Technology Data Exchange (ETDEWEB)

    Masaya, Sugimoto; Koichi, Takeda [Akita Prefectural University (Japan); Solonenko, O.P. [Institute of Theoretical and Applied Mechanics, Novosibirsk (Russian Federation); Sakashita, M.; Nakamura, M. [Japan Technical Information Service, Tokyo (Japan)

    2001-07-01

    Ignition and stable combustion of pulverized coal with Nitrogen and Air plasmas are investigated experimentally for some different types of coal. The experimental results show that air plasma has strong effect for ignition and stabilization of coal combustion. In addition, suppression of NO{sub x} production could be possible even in air plasma. It is possible to ignite and burn stably for the inferior coal that contains volatile matter in the ratio of only 10% of dry total mass. (authors)

  17. BOILER MATERIALS FOR ULTRASUPERCRITICAL COAL POWER PLANTS

    Energy Technology Data Exchange (ETDEWEB)

    R. Viswanathan; K. Coleman; J. Shingledecker; J. Sarver; G. Stanko; M. Borden; W. Mohn; S. Goodstine; I. Perrin

    2005-01-31

    The U.S. Department of Energy (DOE) and the Ohio Coal Development Office (OCDO) have recently initiated a project aimed at identifying, evaluating, and qualifying the materials needed for the construction of the critical components of coal-fired boilers capable of operating at much higher efficiencies than current generation of supercritical plants. This increased efficiency is expected to be achieved principally through the use of ultrasupercritical steam conditions (USC). The project goal initially was to assess/develop materials technology that will enable achieving turbine throttle steam conditions of 760 C (1400 F)/35 MPa (5000 psi), although this goal for the main steam temperature had to be revised down to 732 C (1350 F), based on a preliminary assessment of material capabilities. The project is intended to build further upon the alloy development and evaluation programs that have been carried out in Europe and Japan. Those programs have identified ferritic steels capable of meeting the strength requirements of USC plants up to approximately 620 C (1150 F) and nickel-based alloys suitable up to 700 C (1300 F). In this project, the maximum temperature capabilities of these and other available high-temperature alloys are being assessed to provide a basis for materials selection and application under a range of conditions prevailing in the boiler. This report provides a quarterly status report for the period of July 1 to September 30, 2004.

  18. BOILER MATERIALS FOR ULTRASUPERCRITICAL COAL POWER PLANTS

    Energy Technology Data Exchange (ETDEWEB)

    R. Viswanathan; K. Coleman; J. Shingledecker; J. Sarver; G. Stanko; M. Borden; W. Mohn; S. Goodstine; I. Perrin

    2005-10-27

    The U.S. Department of Energy (DOE) and the Ohio Coal Development Office (OCDO) have recently initiated a project aimed at identifying, evaluating, and qualifying the materials needed for the construction of the critical components of coal-fired boilers capable of operating at much higher efficiencies than current generation of supercritical plants. This increased efficiency is expected to be achieved principally through the use of ultrasupercritical steam conditions (USC). A limiting factor in this can be the materials of construction. The project goal is to assess/develop materials technology that will enable achieving turbine throttle steam conditions of 760 C (1400 F)/35 MPa (5000 psi). This goal seems achievable based on a preliminary assessment of material capabilities. The project is further intended to build further upon the alloy development and evaluation programs that have been carried out in Europe and Japan. Those programs have identified ferritic steels capable of meeting the strength requirements of USC plants up to approximately 620 C (1150 F) and nickel-based alloys suitable up to 700 C (1300 F). In this project, the maximum temperature capabilities of these and other available high-temperature alloys are being assessed to provide a basis for materials selection and application under a range of conditions prevailing in the boiler. This report provides a quarterly status report for the period of July 1 to September 30, 2005.

  19. BOILER MATERIALS FOR ULTRASUPERCRITICAL COAL POWER PLANTS

    Energy Technology Data Exchange (ETDEWEB)

    R. Viswanathan; K. Coleman; J. Shingledecker; J. Sarver; G. Stanko; M. Borden; W. Mohn; S. Goodstine; I. Perrin

    2005-08-01

    The U.S. Department of Energy (DOE) and the Ohio Coal Development Office (OCDO) have recently initiated a project aimed at identifying, evaluating, and qualifying the materials needed for the construction of the critical components of coal-fired boilers capable of operating at much higher efficiencies than current generation of supercritical plants. This increased efficiency is expected to be achieved principally through the use of ultrasupercritical steam conditions (USC). A limiting factor in this can be the materials of construction. The project goal is to assess/develop materials technology that will enable achieving turbine throttle steam conditions of 760 C (1400 F)/35 MPa (5000 psi). This goal seems achievable based on a preliminary assessment of material capabilities. The project is further intended to build further upon the alloy development and evaluation programs that have been carried out in Europe and Japan. Those programs have identified ferritic steels capable of meeting the strength requirements of USC plants up to approximately 620 C (1150 F) and nickel-based alloys suitable up to 700 C (1300 F). In this project, the maximum temperature capabilities of these and other available high-temperature alloys are being assessed to provide a basis for materials selection and application under a range of conditions prevailing in the boiler. This report provides a quarterly status report for the period of April 1 to June 30, 2005.

  20. Boiler Materials for Ultrasupercritical Coal Power Plants

    Energy Technology Data Exchange (ETDEWEB)

    R. Viswanathan; K. Coleman; J. Shingledecker; J. Sarver; G. Stanko; M. Borden; W. Mohn; S. Goodstine; I. Perrin

    2006-07-17

    The U.S. Department of Energy (DOE) and the Ohio Coal Development Office (OCDO) have recently initiated a project aimed at identifying, evaluating, and qualifying the materials needed for the construction of the critical components of coal-fired boilers capable of operating at much higher efficiencies than current generation of supercritical plants. This increased efficiency is expected to be achieved principally through the use of ultrasupercritical steam conditions (USC). A limiting factor in this can be the materials of construction. The project goal is to assess/develop materials technology that will enable achieving turbine throttle steam conditions of 760 C (1400 F)/35 MPa (5000 psi). This goal seems achievable based on a preliminary assessment of material capabilities. The project is further intended to build further upon the alloy development and evaluation programs that have been carried out in Europe and Japan. Those programs have identified ferritic steels capable of meeting the strength requirements of USC plants up to approximately 620 C (1150 F) and nickel-based alloys suitable up to 700 C (1300 F). In this project, the maximum temperature capabilities of these and other available high-temperature alloys are being assessed to provide a basis for materials selection and application under a range of conditions prevailing in the boiler. This report provides a quarterly status report for the period of April 1 to June 30, 2006.

  1. Boiler Materials for Ultrasupercritical Coal Power Plants

    Energy Technology Data Exchange (ETDEWEB)

    R. Viswanathan; K. Coleman; J. Shingledecker; J. Sarver; G. Stanko; M. Borden; W. Mohn; S. Goodstine; I. Perrin

    2006-04-20

    The U.S. Department of Energy (DOE) and the Ohio Coal Development Office (OCDO) have recently initiated a project aimed at identifying, evaluating, and qualifying the materials needed for the construction of the critical components of coal-fired boilers capable of operating at much higher efficiencies than current generation of supercritical plants. This increased efficiency is expected to be achieved principally through the use of ultrasupercritical steam conditions (USC). A limiting factor in this can be the materials of construction. The project goal is to assess/develop materials technology that will enable achieving turbine throttle steam conditions of 760 C (1400 F)/35 MPa (5000 psi). This goal seems achievable based on a preliminary assessment of material capabilities. The project is further intended to build further upon the alloy development and evaluation programs that have been carried out in Europe and Japan. Those programs have identified ferritic steels capable of meeting the strength requirements of USC plants up to approximately 620 C (1150 F) and nickel-based alloys suitable up to 700 C (1300 F). In this project, the maximum temperature capabilities of these and other available high-temperature alloys are being assessed to provide a basis for materials selection and application under a range of conditions prevailing in the boiler. This report provides a quarterly status report for the period of January 1 to March 31, 2006.

  2. Boiler Materials for Ultrasupercritical Coal Power Plants

    Energy Technology Data Exchange (ETDEWEB)

    R. Viswanathan; K. Coleman; J. Shingledecker; J. Sarver; G. Stanko; M. Borden; W. Mohn; S. Goodstine; I. Perrin

    2006-01-31

    The U.S. Department of Energy (DOE) and the Ohio Coal Development Office (OCDO) have recently initiated a project aimed at identifying, evaluating, and qualifying the materials needed for the construction of the critical components of coal-fired boilers capable of operating at much higher efficiencies than current generation of supercritical plants. This increased efficiency is expected to be achieved principally through the use of ultrasupercritical steam conditions (USC). A limiting factor in this can be the materials of construction. The project goal is to assess/develop materials technology that will enable achieving turbine throttle steam conditions of 760 C (1400 F)/35 MPa (5000 psi). This goal seems achievable based on a preliminary assessment of material capabilities. The project is further intended to build further upon the alloy development and evaluation programs that have been carried out in Europe and Japan. Those programs have identified ferritic steels capable of meeting the strength requirements of USC plants up to approximately 620 C (1150 F) and nickel-based alloys suitable up to 700 C (1300 F). In this project, the maximum temperature capabilities of these and other available high-temperature alloys are being assessed to provide a basis for materials selection and application under a range of conditions prevailing in the boiler. This report provides a quarterly status report for the period of October 1 to December 30, 2005.

  3. BOILER MATERIALS FOR ULTRASUPERCRITICAL COAL POWER PLANTS

    Energy Technology Data Exchange (ETDEWEB)

    R. Viswanathan; K. Coleman; J. Shingledecker; J. Sarver; G. Stanko; W. Mohn; M. Borden; S. Goodstine; I. Perrin

    2004-04-23

    The U.S. Department of Energy (DOE) and the Ohio Coal Development Office (OCDO) have recently initiated a project aimed at identifying, evaluating, and qualifying the materials needed for the construction of the critical components of coal-fired boilers capable of operating at much higher efficiencies than current generation of supercritical plants. This increased efficiency is expected to be achieved principally through the use of ultrasupercritical steam conditions (USC). The project goal initially was to assess/develop materials technology that will enable achieving turbine throttle steam conditions of 760 C (1400 F)/35 MPa (5000 psi), although this goal for the main steam temperature had to be revised down to 732 C (1350 F), based on a preliminary assessment of material capabilities. The project is intended to build further upon the alloy development and evaluation programs that have been carried out in Europe and Japan. Those programs have identified ferritic steels capable of meeting the strength requirements of USC plants up to approximately 620 C (1150 F) and nickel-based alloys suitable up to 700 C (1300 F). In this project, the maximum temperature capabilities of these and other available high-temperature alloys are being assessed to provide a basis for materials selection and application under a range of conditions prevailing in the boiler. This report provides a quarterly status report for the period of October 1 to December 30, 2003.

  4. BOILER MATERIALS FOR ULTRASUPERCRITICAL COAL POWER PLANTS

    Energy Technology Data Exchange (ETDEWEB)

    R. Viswanathan; K. Coleman; J. Shingledecker; J. Sarver; G. Stanko; W. Mohn; M. Borden; S. Goodstine; I. Perrin

    2004-07-30

    The U.S. Department of Energy (DOE) and the Ohio Coal Development Office (OCDO) have recently initiated a project aimed at identifying, evaluating, and qualifying the materials needed for the construction of the critical components of coal-fired boilers capable of operating at much higher efficiencies than current generation of supercritical plants. This increased efficiency is expected to be achieved principally through the use of ultrasupercritical steam conditions (USC). The project goal initially was to assess/develop materials technology that will enable achieving turbine throttle steam conditions of 760 C (1400 F)/35 MPa (5000 psi), although this goal for the main steam temperature had to be revised down to 732 C (1350 F), based on a preliminary assessment of material capabilities. The project is intended to build further upon the alloy development and evaluation programs that have been carried out in Europe and Japan. Those programs have identified ferritic steels capable of meeting the strength requirements of USC plants up to approximately 620 C (1150 F) and nickel-based alloys suitable up to 700 C (1300 F). In this project, the maximum temperature capabilities of these and other available high-temperature alloys are being assessed to provide a basis for materials selection and application under a range of conditions prevailing in the boiler. This report provides a quarterly status report for the period of April to June 30, 2004.

  5. Boiler Materials For Ultrasupercritical Coal Power Plants

    Energy Technology Data Exchange (ETDEWEB)

    R. Viswanathan; K. Coleman; J. Shingledecker; J. Sarver; G. Stanko; M. Borden; W. Mohn; S. Goodstine; I. Perrin

    2006-09-30

    The U.S. Department of Energy (DOE) and the Ohio Coal Development Office (OCDO) have recently initiated a project aimed at identifying, evaluating, and qualifying the materials needed for the construction of the critical components of coal-fired boilers capable of operating at much higher efficiencies than current generation of supercritical plants. This increased efficiency is expected to be achieved principally through the use of ultrasupercritical steam conditions (USC). A limiting factor in this can be the materials of construction. The project goal is to assess/develop materials technology that will enable achieving turbine throttle steam conditions of 760 C (1400 F)/35 MPa (5000 psi). This goal seems achievable based on a preliminary assessment of material capabilities. The project is further intended to build further upon the alloy development and evaluation programs that have been carried out in Europe and Japan. Those programs have identified ferritic steels capable of meeting the strength requirements of USC plants up to approximately 620 C (1150 F) and nickel-based alloys suitable up to 700 C (1300 F). In this project, the maximum temperature capabilities of these and other available high-temperature alloys are being assessed to provide a basis for materials selection and application under a range of conditions prevailing in the boiler. This report provides a quarterly status report for the period of July 1 to September 30, 2006.

  6. A New Agro/Forestry Residues Co-Firing Model in a Large Pulverized Coal Furnace: Technical and Economic Assessments

    Directory of Open Access Journals (Sweden)

    Shien Hui

    2013-08-01

    Full Text Available Based on the existing biomass co-firing technologies and the known innate drawbacks of dedicated biomass firing, including slagging, corrosion and the dependence on fuel, a new model of agro/forestry residue pellets/shreds and coal co-fired in a large Pulverized Coal (PC furnace was proposed, and the corresponding technical and economic assessments were performed by co-firing testing in a 300 MW PC furnace and discounted cash flow technique. The developed model is more dependent on injection co-firing and combined with co-milling co-firing. Co-firing not only reduces CO2 emission, but also does not significantly affect the fly ash use in cement industry, construction industry and agriculture. Moreover, economic assessments show that in comparison with dedicated firing in grate furnace, agro/forestry residues and coal co-firing in a large PC furnace is highly economic. Otherwise, when the co-firing ratio was below 5 wt%, the boiler co-firing efficiency was 0.05%–0.31% higher than that of dedicated PC combustion, and boiler efficiencies were about 0.2% higher with agro/forestry residues co-firing in the bottom and top burner systems than that in a middle burner system.

  7. A Model for Nitrogen Chemistry in Oxy-Fuel Combustion of Pulverized Coal

    OpenAIRE

    Hashemi, Hamid; Hansen, Stine; Toftegaard, Maja Bøg; Pedersen, Kim Hougaard; Jensen, Anker Degn; Dam-Johansen, Kim; Glarborg, Peter

    2011-01-01

    In this work, a model for the nitrogen chemistry in the oxy-fuel combustion of pulverized coal has been developed. The model is a chemical reaction engineering type of model with a detailed reaction mechanism for the gas-phase chemistry, together with a simplified description of the mixing of flows, heating and devolatilization of particles, and gas–solid reactions. The model is validated by comparison with entrained flow reactor results from the present work and from the literature on pulver...

  8. High gradient magnetic beneficiation of dry pulverized coal via upwardly directed recirculating fluidization

    Science.gov (United States)

    Eissenberg, David M.; Liu, Yin-An

    1980-01-01

    This invention relates to an improved device and method for the high gradient magnetic beneficiation of dry pulverized coal, for the purpose of removing sulfur and ash from the coal whereby the product is a dry environmentally acceptable, low-sulfur fuel. The process involves upwardly directed recirculating air fluidization of selectively sized powdered coal in a separator having sections of increasing diameters in the direction of air flow, with magnetic field and flow rates chosen for optimum separations depending upon particulate size.

  9. Gasification in pulverized coal flames. First annual progress report, July 1975--June 1976

    Energy Technology Data Exchange (ETDEWEB)

    Lenzer, R. C.; George, P. E.; Thomas, J. F.; Laurendeau, N. M.

    1976-07-01

    This project concerns the production of power and synthesis gas from pulverized coal via suspension gasification. Swirling flow in both concentric jet and cyclone gasifiers will separate oxidation and reduction zones. Gasifier performance will be correlated with internally measured temperature and concentration profiles. A literature review of vortex and cyclone reactors is complete. Preliminary reviews of confined jet reactors and pulverized coal reaction models have also been completed. A simple equilibrium model for power gas production is in agreement with literature correlations. Cold gas efficiency is not a suitable performance parameter for combined cycle operation. The coal handling facility, equipped with crusher, pulverizer and sieve shaker, is in working order. Test cell flow and electrical systems have been designed, and most of the equipment has been received. Construction of the cyclone gasifier has begun. A preliminary design for the gas sampling system, which will utilize a UTI Q-30C mass spectrometer, has been developed.

  10. Numerical study of co-firing pulverized coal and biomass inside a cement calciner.

    Science.gov (United States)

    Mikulčić, Hrvoje; von Berg, Eberhard; Vujanović, Milan; Duić, Neven

    2014-07-01

    The use of waste wood biomass as fuel is increasingly gaining significance in the cement industry. The combustion of biomass and particularly co-firing of biomass and coal in existing pulverized-fuel burners still faces significant challenges. One possibility for the ex ante control and investigation of the co-firing process are computational fluid dynamics (CFD) simulations. The purpose of this paper is to present a numerical analysis of co-firing pulverized coal and biomass in a cement calciner. Numerical models of pulverized coal and biomass combustion were developed and implemented into a commercial CFD code FIRE, which was then used for the analysis. Three-dimensional geometry of a real industrial cement calciner was used for the analysis. Three different co-firing cases were analysed. The results obtained from this study can be used for assessing different co-firing cases, and for improving the understanding of the co-firing process inside the calculated calciner.

  11. Cold Gas-particle Flows in a New Swirl Pulverized-coal Burner by PDPA Measurement

    Institute of Scientific and Technical Information of China (English)

    2000-01-01

    A new type of swirl burner has been developed to stabilize pulverized-coal combustion by burning different types of coal at different loads and to reduce NOx formation during combustion. The burner uses a device to concentrate the coal powder in the primary-air tube that divides the primary coal-air into two streams with different pulverized-coal concentrations. This paper reports the measurement of gas-particle flows at the exit of the different swirl burners using a 3-D Phase Doppler Particle Anemometer (PDPA). The effect of different geometrical configurations on the two-phase flow field is studied. The results that give the two-phase flow fields and particle concentrations show the superiority of the new swirl burner.

  12. Technological Analysis on Choren High-Pressure Pulverized Coal Gasification Process%科林高压干粉煤气化工艺技术分析

    Institute of Scientific and Technical Information of China (English)

    赵小倩; 胡长胜

    2011-01-01

    The process and features of Choren high-pressure pulveried coal gasification are presented. Operability of the gasification technology is analysed. And the operation data as compared with the other two coal gasification processes, i.e. pulverized coal gasification process with waste heat boiler and coal-water slurry pressure gasification process, using in China are described briefly. Choren high-pressure pulverized coal gasification process is featured with simple in equipment structure, wider applicability of coal variety, lower consumption and high localization of equipment.%介绍了科林高压干粉煤气化的工艺流程、工艺特点.对该气化技术的可操作性进行了分析,并与国内应用的2种煤气化工艺(干粉煤废锅气化工艺和水煤浆加压气化工艺)数据进行了简单对比.科林高压干粉煤气化工艺具有设备结构简单、煤种适用性更宽、消耗低和设备国产化程度高的特点.

  13. The effect of fuel form on trace element emissions in an industrial-scale coal fired boiler

    Energy Technology Data Exchange (ETDEWEB)

    Miller, S.F.; Wincek, R.T.; Miller, B.G.; Scaroni, A.W. [Pennsylvania State Univ., University Park, PA (United States). Coal Utilization Lab.

    1998-12-31

    Eleven of the fourteen inorganic hazardous air pollutants identified in Title 3 of the Clean Air Act Amendments of 1990 are present in the flue gas of pulverized coal-fired boilers. The designated elements include: antimony (Sb), beryllium (Be), chlorine (Cl), cobalt (Co), manganese (Mn), nickel (Ni), selenium (Se), fluorine (F), arsenic (As), cadmium (Cd), chromium (Cr), lead (Pb), mercury (Hg), and phosphorus (P). Determining the risk of these elements in the environment is difficult at best. However, regulating their emission into the environment has some scientific basis and merit. Approximately 137.5 tons of mercury were emitted in the US by combustion sources in 1994--1995, with coal-fired utility boilers accounting for 37.4% (or 51.6 tons) of the total. Control of trace element emissions from coal-fired utility boilers requires an understanding of the manner in which they occur in coal, their behavior during and after combustion and their form in the stack gas. The multimedia behavior of trace elements during combustion can be traced to their volatility within the combustion and post-combustion environment. The temperature distribution within the combustion system, the mechanism of char and ash formation (e.g. duration of char burnout and char and cenosphere morphology) and the combustion efficiency determine the partitioning of trace elements during combustion. These factors can be affected by the form in which a fuel is fired, e.g., pulverized coal (PC) versus coal-water slurry fuel (CWSF). This paper presents preliminary results of emissions testing aimed at determining the effect of fuel form on the penetration and partitioning of trace elements in an industrial-scale boiler. The tests were conducted on a 2 MMBtu/hr research boiler, in which Middle Kittanning Seam coal (hvA bituminous) from Jefferson County, Pennsylvania was burned in pulverized form and as a CWSF. The tests were conducted in accordance with the procedure outlined in EPA Methods 5 and 29

  14. Effect of multiphase radiation on coal combustion in a pulverized coal jet flame

    Science.gov (United States)

    Wu, Bifen; Roy, Somesh P.; Zhao, Xinyu; Modest, Michael F.

    2017-08-01

    The accurate modeling of coal combustion requires detailed radiative heat transfer models for both gaseous combustion products and solid coal particles. A multiphase Monte Carlo ray tracing (MCRT) radiation solver is developed in this work to simulate a laboratory-scale pulverized coal flame. The MCRT solver considers radiative interactions between coal particles and three major combustion products (CO2, H2O, and CO). A line-by-line spectral database for the gas phase and a size-dependent nongray correlation for the solid phase are employed to account for the nongray effects. The flame structure is significantly altered by considering nongray radiation and the lift-off height of the flame increases by approximately 35%, compared to the simulation without radiation. Radiation is also found to affect the evolution of coal particles considerably as it takes over as the dominant mode of heat transfer for medium-to-large coal particles downstream of the flame. To investigate the respective effects of spectral models for the gas and solid phases, a Planck-mean-based gray gas model and a size-independent gray particle model are applied in a frozen-field analysis of a steady-state snapshot of the flame. The gray gas approximation considerably underestimates the radiative source terms for both the gas phase and the solid phase. The gray coal approximation also leads to under-prediction of the particle emission and absorption. However, the level of under-prediction is not as significant as that resulting from the employment of the gray gas model. Finally, the effect of the spectral property of ash on radiation is also investigated and found to be insignificant for the present target flame.

  15. Slagging in a pulverised-coal-fired boiler

    Energy Technology Data Exchange (ETDEWEB)

    Devir, G.P.; Pohl, J.H.; Creelman, R.A. [University of Queensland, St. Lucia, Qld. (Australia). Dept. of Chemical Engineering

    2000-07-01

    This paper describes a technique to evaluate the severity of slagging of a coal in a pulverised-coal-fired boiler. There are few data in the literature on the nature of in-situ boiler slags, their rate of growth and/or their strength properties relevant to sootblowing. The latter is thought to be of more concern to boiler operators and gives rise to the significance of selecting suitable strength tests. As well as standardised methods for characterising pulverised coal performance in a boiler, several novel and less popular techniques are discussed in detail. A suite of three sub-bituminous coals from the Callide Coalfields, Biloela (600 km north of Brisbane), has been selected for slagging tests in the 350 MW{sub e} units of Callide 'B' power station. Disposable air-cooled mild steel slagging probes have been constructed to simulate the conditions for deposit formation in the boiler region. To date, tests for one of these coals has been completed and preliminary results are presented. Once testing for the remaining coals has been completed, it is anticipated that the differences exhibited in deposit growth and strength may be correlated with typical variations in physical and chemical properties of the pulverised coal.

  16. Computational fluid dynamics (CFD) analysis of the coal combustion in a boiler of a thermal power plant using different kinds of the manufactured coals

    Energy Technology Data Exchange (ETDEWEB)

    Silva, Cristiano Vitorino da; Lazzari, Luis Carlos; Ziemniczak, Aline; Beskow, Arthur Bortolin [Universidade Regional Integrada do Alto Uruguai e das Missoes (URI), Erechim, RS (Brazil)], E-mails: cristiano@uricer.edu.br, arthur@uricer.edu.br

    2010-07-01

    The state of the art in computational fluid dynamics and the availability of commercial codes encourage numerical studies of combustion processes. In the present work the commercial software CFX Ansys Europe Ltd. has been used to study the combustion of pulverized coal into the boiler of a thermal power plant. The objective of this work is to obtain new information for process optimization. Different kinds of manufactured coals were numerically tested in a thermal power plant installed at the southeast region of Brazil. The simulations were made using the actual burning conditions of the boiler. Results include the residence time of the fuel into the combustion chamber, temperature fields, flow fluid mechanics, heat transfer and pollutant formation, as well as the CO and NOx concentrations, aiming to determinate the best conditions to burn the investigated coals. The numerical investigation of the phenomena involved on the coal combustion processes are used to complete the experimental information obtained in operational tests. Considering the characteristics of different kinds of manufactured coals used, with this study is possible to achieve the most efficient boiler operation parameters, with decreasing costs of electricity production and reduction of environmentally harmful emissions. It was verified that the different kinds of manufactured coals demand different operation conditions, and the kind of manufactured coal used on the combustion process has a significant effect on the pollutant formation, mainly in rel action with ash concentration. (author)

  17. A novel model for cost performance evaluation of pulverized coal injected into blast furnace based on effective calorific value

    Institute of Scientific and Technical Information of China (English)

    徐润生; 张建良; 左海滨; 李克江; 宋腾飞; 邵久刚

    2015-01-01

    The combustion process of pulverized coal injected into blast furnace involves a lot of physical and chemical reactions. Based on the combustion behaviors of pulverized coal, the conception of coal effective calorific value representing the actual thermal energy provided for blast furnace was proposed. A cost performance evaluation model of coal injection was built up for the optimal selection of various kinds of coal based on effective calorific value. The model contains two indicators: coal effective calorific value which has eight sub-indicators and coal injection cost which includes four sub-indicators. In addition, the calculation principle and application of cost performance evaluation model in a Chinese large-scale iron and steel company were comprehensively introduced. The evaluation results finally confirm that this novel model is of great significance to the optimal selection of blast furnace pulverized coal.

  18. SRC burn test in 700-hp oil-designed boiler. Volume 2. Engineering evaluation report. Final technical report. [Oil-fired boiler to solvent-refined coal

    Energy Technology Data Exchange (ETDEWEB)

    1983-12-01

    Volume 2 of this report gives the results of an engineering evaluation study and economic analysis of converting an existing 560-MW residual (No. 6) oil-fired unit to burn solvent refined coal (SRC) fuel forms. Volume 1 represents an integrated overview of the test program conducted at the Pittsburgh Energy Technology Center. Three SRC forms (pulverized SRC, a solution of SRC dissolved in process-derived distillates, and a slurry of SRC and water) were examined. The scope of modifications necessary to convert the unit to each of the three SRC fuel forms was identified and a capital cost of the necessary modifications estimated. A fuel conversion feasibility study of the boiler was performed wherein boiler modifications and performance effects of each fuel on the boiler were identified. An economic analysis of the capital and operating fuel expenses of conversion of the unit was performed. It was determined that conversion of the unit to any one of the three SRC fuel forms was feasible where appropriate modifications were made. It also was determined that the conversion of the unit can be economically attractive if SRC fuel forms can be manufactured and sold at prices discounted somewhat from the price of No. 16 Fuel Oil. As expected, greater discounts are required for the pulverized SRC and the slurry than for the solution of SRC dissolved in process-derived distillates.

  19. Investigation on Pulverized Coal Combustion Behavior by Non-Isothermic Integral Thermogravimetry Method

    Institute of Scientific and Technical Information of China (English)

    QI Cheng-lin; ZHANG Jian-liang; LIN Xiang-hai; LIU Qin-yuan; WANG Xiao-liu

    2011-01-01

    The combustion process of pulverized coal was investigated by non-isothermic integral thermogravimetry. The thermogravimetry curves were fitted by the Coats-Redferm approximation function, and kinetic parameters and characteristic temperatures were obtained. The optimal mixing ratio and particle size can be ascertained. The characteristic temperature of pulverized coal can be obtained from the thermogravimetry curve, and the combustion of coal can be divided into homogeneous and heterogeneous combustion according to the differential thermal analysis curve. The activation energy of a single type of coal ranking from low to high is as follows: bituminous coal, meager-lean coal, and anthracite. In the first mixing method, with more low-price meager-lean coal B replacing high price anthracite A, the activation energy slightly decreases; with more bituminous coal replacing meager-lean coal, total tendency makes a declining of activation. In the later mixing method, with an increase in particle size, a declining activation energy can be seen in total tendency.

  20. Pulverized coal injection in blast furnaces at ArcelorMittal Tubarao (AMT)

    Energy Technology Data Exchange (ETDEWEB)

    Klein, C.A.; Fujihara, F.K.; Defendi, G.A.; Tauffer Barros, R.J. [ArcelorMittal Tubarao, Serra (Brazil). Ironmaking Dept.

    2008-07-01

    The main factors that influence the performance of coal injected into blast furnaces include coal properties, combustion conditions and the equipment used in the plants for grinding, transportation and injection of coal. This paper focused on coal properties and the main operational control changes in the no.1 blast furnace at ArcelorMittal Tubarao. The furnace was modified from an all coke operation to a pulverized coal injection (pci) operation in order to ensure high productivity, low fuel consumption and longer service life. ArcelorMittal Tubarao has developed a coal buying model based on energy balance and the chemical analysis of ash. In the energy balance, the ratio between the heat supplied by carbon combustion and the heat consumed by the cracking of water and volatiles results in the potential rate of coke replacement by coal. 5 refs., 1 tab., 10 figs.

  1. The behaviour of coal blends in power station boilers

    Energy Technology Data Exchange (ETDEWEB)

    Livingston, W.R.; Horne, P.A.; McGhee, B.F.; Gibson, J.R. [Mitsui Babcock Energy Ltd., Renfrew (United Kingdom)

    1998-12-31

    The milling characteristics of coal blends were studied to provide quantitative information which allows the calculation of the Hardgrove Index (HGI) values of coal blends from those of the constituent coals; to provide data on the power requirement to produce a given mill output fineness, and abrasion rates of mill components when milling coal blends, relative to the behaviour of the constituent coals; to investigate the combustion behaviour of coal blends in pulverized fuel-fired systems by carrying out testwork in a semi-industrial combustion test facility, and to assess the deposition characteristics and the potential for utilization of the ashes produced by the combustion of coal blends. It was found that both the HGI and the Abrasion Index values of coals are additive properties. There were linear correlations between the slope of the Rosin-Rammler plot of the Mini-mill product size distribution and both the blend compositions and the HGI values of the coals and coal blends. Investigations showed that the fusion behaviour of the coal ash blends is rather complex, and that the characteristic ash fusion temperature are not additive in a simple way. A number of correlations were found between the ash fusion temperatures of the coals and coal ash blends. 1 ref., 45 figs., 10 tabs., 1 app.

  2. Industrial Experimental Study and Application of Plasma Pulverized Coal Ignition Burner%等离子煤粉点火燃烧器工业性试验研究及应用

    Institute of Scientific and Technical Information of China (English)

    崔凤誉; 张玉周

    2001-01-01

    This paper systematically explains the content and method of industrial experiment in plasma pulverized coal ignition burner analyzes the experiment results,and puts forward the two-parameter concentration of pulverized coal and fuel ratio combustion regulation-control of plasma pulverized coal ignition burner.On the basis of the industrial experiment,Shandong Yantai Coal-fired Power Plant has realized successfully the boiler ignition without oil aid by using plasma pulverized coal ignition burner for the first time.%阐释等离子煤粉点火燃烧器工业试验的内容及方法,并对其试验结果进行分析。提出等离子煤粉点火燃烧器燃烧调整的双参数煤粉浓度、燃功比控制法。在对等离子煤粉点火燃烧器工业试验基础上,2000年2月15日,山东烟台发电厂利用等离子煤粉点火燃烧器首次实现了机组无油点火。

  3. Pulverized coal burnout in blast furnace simulated by a drop tube furnace

    Energy Technology Data Exchange (ETDEWEB)

    Du, Shan-Wen [Steel and Aluminum Research and Development Department, China Steel Corporation, Kaohsiung 812 (China); Chen, Wei-Hsin [Department of Greenergy, National University of Tainan, Tainan 700 (China); Lucas, John A. [School of Engineering of the University of Newcastle, Callaghan, NSW 2308 (Australia)

    2010-02-15

    Reactions of pulverized coal injection (PCI) in a blast furnace were simulated using a drop tube furnace (DTF) to investigate the burnout behavior of a number of coals and coal blends. For the coals with the fuel ratio ranging from 1.36 to 6.22, the experimental results indicated that the burnout increased with decreasing the fuel ratio, except for certain coals departing from the general trend. One of the coals with the fuel ratio of 6.22 has shown its merit in combustion, implying that the blending ratio of the coal in PCI operation can be raised for a higher coke replacement ratio. The experiments also suggested that increasing blast temperature was an efficient countermeasure for promoting the combustibility of the injected coals. Higher fuel burnout could be achieved when the particle size of coal was reduced from 60-100 to 100-200 mesh. However, once the size of the tested coals was in the range of 200 and 325 mesh, the burnout could not be improved further, resulting from the agglomeration of fine particles. Considering coal blend reactions, the blending ratio of coals in PCI may be adjusted by the individual coal burnout rather than by the fuel ratio. (author)

  4. Impact of petrographic properties on the burning behavior of pulverized coal using a drop tube furnace

    Energy Technology Data Exchange (ETDEWEB)

    S. Biswas; N. Choudhury; S. Ghosal; T. Mitra; A. Mukherjee; S.G. Sahu; M. Kumar [Jadavpur University, Dhanbad (India). Central Fuel Research Institute]. sb_cfri@yahoo.co.in

    2007-12-15

    The combustion behavior of three Indian coals of different rank with wide variation in ash content and maceral compositions were studied using a drop tube furnace (DTF). Each coal was pulverized into a specific size (80% below 200 mesh) and fed into the DTF separately. The DTF runs were carried out under identical conditions for all of the coals. The carbon burnout was found out from the chemical analyses of the feed coals and the char samples collected from different ports of the DTF. Char morphology analyses was carried on the burnout residues of the top port. The top port results show better burnout of the lower rank coals which however was not observed in the last port. An attempt has been made to account for this variation in terms of rank and petrographic parameters of the respective coals. 20 refs., 1 fig., 6 tabs.

  5. Pulverized coal and substitute fuels for the cement manufacturing industry

    Energy Technology Data Exchange (ETDEWEB)

    Dobrowsky, F.

    1981-01-01

    This paper comprises an article of general technical interest on coal and its use in the cement industry, plus the scope for using substitute fuels. Discusses coal properties and preparation (crushing). Describes the heating systems of the cement ovens: burners, combustion and parameters governing flame-length. Looks at operation problems connected with heating of the coal: caking, fusing, clinker quality and behaviour of the refractory bricks. Also discusses substitute fuels: type of fuel, scope for utilisation and requisite precautions. 32 refs.

  6. The Influencing Factors and Countermeasures for Self-ignition of Pulverized Coal Warehouse in Pulverized Coal Milling System%中间储仓式制粉系统粉仓自燃影响因素及对策

    Institute of Scientific and Technical Information of China (English)

    金帆; 李善涛

    2012-01-01

    针对中国石化上海石油化工股份有限公司热电部410 t/h煤粉炉在停炉抢修期间中间储仓式的粉仓内温度急剧上升、煤粉自燃的现象,分析了引起煤粉自燃的影响因素。根据实际情况,提出了煤粉自燃的防治措施和预防粉仓温度升高的方法。%Regarding the quick rising of temperature in the middle-warehouse pulverized coal house and self-ignition of pulverized coal in 410 t/a pulverized coal furnace during shutdown and emergency repairing period,the influencing factors causing self-ignition of pulverized coal were analyzed.Based on the practical situation,the preventions for self-ignition of pulverized coal and methods for preventing temperature in pulverized coal house from rising were raised.

  7. Modeling of pulverized coal combustion processes in a vortex furnace of improved design. Part 2: Combustion of brown coal from the Kansk-Achinsk Basin in a vortex furnace

    Science.gov (United States)

    Krasinsky, D. V.; Salomatov, V. V.; Anufriev, I. S.; Sharypov, O. V.; Shadrin, E. Yu.; Anikin, Yu. A.

    2015-03-01

    This paper continues with the description of study results for an improved-design steam boiler vortex furnace, for the full-scale configuration of which the numerical modeling of a three-dimensional turbulent two-phase reacting flow has been performed with allowance for all the principal heat and mass transfer processes in the torch combustion of pulverized Berezovsk brown coal from the Kansk-Achinsk Basin. The detailed distributions of velocity, temperature, concentration, and heat flux fields in different cross sections of the improved vortex furnace have been obtained. The principal thermoengineering and environmental characteristics of this furnace are given.

  8. Relationship between Particle Size Distribution of Low-Rank Pulverized Coal and Power Plant Performance

    Directory of Open Access Journals (Sweden)

    Rajive Ganguli

    2012-01-01

    Full Text Available The impact of particle size distribution (PSD of pulverized, low rank high volatile content Alaska coal on combustion related power plant performance was studied in a series of field scale tests. Performance was gauged through efficiency (ratio of megawatt generated to energy consumed as coal, emissions (SO2, NOx, CO, and carbon content of ash (fly ash and bottom ash. The study revealed that the tested coal could be burned at a grind as coarse as 50% passing 76 microns, with no deleterious impact on power generation and emissions. The PSD’s tested in this study were in the range of 41 to 81 percent passing 76 microns. There was negligible correlation between PSD and the followings factors: efficiency, SO2, NOx, and CO. Additionally, two tests where stack mercury (Hg data was collected, did not demonstrate any real difference in Hg emissions with PSD. The results from the field tests positively impacts pulverized coal power plants that burn low rank high volatile content coals (such as Powder River Basin coal. These plants can potentially reduce in-plant load by grinding the coal less (without impacting plant performance on emissions and efficiency and thereby, increasing their marketability.

  9. 低挥发分煤粉燃烧新技术发展与应用%Development and application of low volatile pulverized coal combustion technique

    Institute of Scientific and Technical Information of China (English)

    周建明

    2011-01-01

    Introduce the development and application of low volatile pulverized coal combustion technique. The representative burners and framework of boilers were demonstrated and the key techniques, including strengthening hot gas back flow,keeping adopting pulverized coal concentration,and extending length of flame,were also analyzed and these techniques can help pulverized coal ignite quickly and keep stable ignition. The suitable combustion system should be strictly chosen for low volatilization pulverized coal, such as tangentially firing, opposed firing, W-shape flame, and CUF firing and so on. Meanwhile, being the superior stability in anthracite combustion to tangential firing and opposed firing,W-shape boilers are mainly used. Having the strongpoint of stable combustion, high combustion efficiency, stepped firing in recirculation and low NO, emission, the high-temperature combustion technique for low volatilization coal will have wide application foreground.%介绍了国内外低挥发分煤粉燃烧技术及发展.对具有代表性的燃烧器及炉膛结构进行简要分析,说明热回流、煤粉浓缩、延长火焰长度等关键技术在实现低挥发分难燃煤粉快速着火、稳定燃烧中的应用.指出尽管燃烧器在应用中取得一定的效果,但仍然存在一些问题,因而对于低挥发分煤种还需要同时选择合理的燃烧方式,如切向燃烧、对冲燃烧、W型火焰燃烧及CUF火焰燃烧等技术.其中,W型火焰燃烧方式对难燃无烟煤的燃烧稳定性优于四角和对冲燃烧方式,是目前主要采用的燃烧结构.高温空气燃烧技术对低挥发分煤具有火焰稳定、热效率高、再循环分级燃烧,低NOx排放等优点,将成为更有前景的燃烧技术.

  10. Analysis of Chemical Reaction Kinetics Behavior of Nitrogen Oxide During Air-staged Combustion in Pulverized Boiler

    Directory of Open Access Journals (Sweden)

    Jun-Xia Zhang

    2016-03-01

    Full Text Available Because the air-staged combustion technology is one of the key technologies with low investment running costs and high emission reduction efficiency for the pulverized boiler, it is important to reveal the chemical reaction kinetics mechanism for developing various technologies of nitrogen oxide reduction emissions. At the present work, a three-dimensional mesh model of the large-scale four corner tangentially fired boiler furnace is established with the GAMBIT pre-processing of the FLUENT software. The partial turbulent premixed and diffusion flame was simulated for the air-staged combustion processing. Parameters distributions for the air-staged and no the air-staged were obtained, including in-furnace flow field, temperature field and nitrogen oxide concentration field. The results show that the air-staged has more regular velocity field, higher velocity of flue gas, higher turbulence intensity and more uniform temperature of flue gas. In addition, a lower negative pressure zone and lower O2 concentration zone is formed in the main combustion zone, which is conducive to the NO of fuel type reduced to N2, enhanced the effect of NOx reduction. Copyright © 2016 BCREC GROUP. All rights reserved Received: 5th November 2015; Revised: 14th January 2016; Accepted: 16th January 2016  How to Cite: Zhang, J.X., Zhang, J.F. (2016. Analysis of Chemical Reaction Kinetics Behavior of Nitrogen Oxide During Air-staged Combustion in Pulverized Boiler. Bulletin of Chemical Reaction Engineering & Catalysis, 11 (1: 100-108. (doi:10.9767/bcrec.11.1.431.100-108 Permalink/DOI: http://dx.doi.org/10.9767/bcrec.11.1.431.100-108

  11. Anatomy of an upgraded pulverized coal facility: Combustion modification through flue gas scrubbing

    Energy Technology Data Exchange (ETDEWEB)

    Watts, J.U. [Dept. of Energy, Pittsburgh, PA (United States). Federal Energy Technology Center; Savichky, W.J.; O`Dea, D.T. [New York State Electric and Gas Corp., Binghamton, NY (United States)

    1997-12-31

    Regeneration is a biological term for formation or creating anew. In the case of Milliken station, a species of steam generation (Tangentus coali) regeneration refers to refitting critical systems with the latest technological advances to reduce emissions while maintaining or improving performance. The plant has undergone a series of operations which provided anatomical changes as well as a face lift. Each of the two units were place in suspended animation (outage) to allow these changes to be made. The paper describes the project which includes retrofitting combustion systems, pulverizers, boiler liners, scrubbers, and control room. This retrofit is meant to increase thermal efficiency while reducing the formation of nitrogen oxides.

  12. On-line tracking of pulverized coal and biomass fuels through flame spectrum analysis

    Institute of Scientific and Technical Information of China (English)

    迟天阳; 张宏建

    2007-01-01

    This paper presents a new approach to the on-line tracking of pulverized coal and biomass fuels through flame spectrum analysis. A flame detector containing four photodiodes is used to derive multiple signals covering a wide spectrum of the flame from visible, near-infrared and mid-infrared spectral bands as well as a part of far-infrared band. Different features are extracted in time and frequency domains to identify the dynamic "fingerprints" of the flame. Fuzzy logic inference techniques are employed to combine typical features together and infer the type of fuel being burnt. Four types of pulverized coal and five types of biomass are burnt on a laboratory-scale combustion test rig. Results obtained demonstrate that this approach is capable of tracking the type of fuel under steady combustion conditions.

  13. Energy Analysis of a Biomass Co-firing Based Pulverized Coal Power Generation System

    Directory of Open Access Journals (Sweden)

    Marc A. Rosen

    2012-03-01

    Full Text Available The results are reported of an energy analysis of a biomass/coal co-firing based power generation system, carried out to investigate the impacts of biomass co-firing on system performance. The power generation system is a typical pulverized coal-fired steam cycle unit, in which four biomass fuels (rice husk, pine sawdust, chicken litter, and refuse derived fuel and two coals (bituminous coal and lignite are considered. Key system performance parameters are evaluated for various fuel combinations and co-firing ratios, using a system model and numerical simulation. The results indicate that plant energy efficiency decreases with increase of biomass proportion in the fuel mixture, and that the extent of the decrease depends on specific properties of the coal and biomass types.

  14. Adapter for converting an oil burner head for burning of pulverized coal

    Energy Technology Data Exchange (ETDEWEB)

    Musil, J.E.

    1988-03-29

    This patent describes a burner head means forming a primary air passage in the burner head including a portion of generally circular configuration in cross-section having openings uniformally circularly disposed about its periphery, and a manifold effective to envelope the primary air passage means. The manifold has inlet means for connection to a source of pulverized coal and air, internal coal and air passages downstream of the inlet effective to divide incoming coal and air into a plurality of discrete streams thereof, and a manifold coal and air outlet opening from each coal and air passage. The manifold outlet openings each are in communication with a duct means having an outlet discharging into one of the openings about the periphery of the primary air passage means.

  15. Fundamentals of the physical-chemistry of pulverized coal combustion

    Energy Technology Data Exchange (ETDEWEB)

    Lahaye, J.; Prado, G. (eds.)

    1987-01-01

    A total of 20 papers were presented at the conference in seven sessions the major headings of which are: devolatilization, heterogeneous combustion, pollutants in coal combustion, optical diagnostics and transfer to the modelling.

  16. Analysis of the Common Faults of Coal Pulverizing System of Thermal Power Plant%火力电厂制粉系统常见故障分析

    Institute of Scientific and Technical Information of China (English)

    李炀文; 张超; 刘学伟

    2014-01-01

    Mill is the coal drying and grinding into qualified coal fineness to the boiler burner, the boiler to meet the load de-mand of machinery. ZGM-123G type coal pulverizer is a kind of medium speed coal mill of type system, its advantages of sim-ple, compact layout, power consumption is low, the disadvantage is the requirement to control boiler operation, such as milling system fault is a direct threat to the normal operation of the boiler. Abnormal phenomenon it is necessary to often happen on mill-ing system in the production process and the reason to make the summary, and put forward the accident processing method.%磨煤机是将原煤经干燥和碾磨后制成细度合格的煤粉送到锅炉燃烧器,以满足锅炉负荷的需求的机械。ZGM-123G型磨煤机是一种中速辊盘式磨煤机,其优点系统简单,布置紧凑,运行电耗也较低,缺点是对锅炉运行操作控制要求高,如制粉系统中出现故障就直接威胁到锅炉的正常运行。因此有必要对生产过程中制粉系统常发生的异常现象及原因做出总结,并针对性提出事故处理方法。

  17. Mitsubishi latest coal fired USC boiler technology (CFE Pacifico 700 MW)

    Energy Technology Data Exchange (ETDEWEB)

    Hashimoto, T.; Sakamoto, K. [Mitsubishi Heavy Industries, Ltd., Nagasaki (Japan). Power Systems; Fujitab, M. [Mitsubishi Heavy Industries, Ltd., Yokohama (Japan). Power Systems

    2013-07-01

    Mitsubishi Heavy Industries, Ltd. (MHI) has successfully completed commissioning work for CFE (Comision Federal de Electricidad) Pacifico 700 MW coal-fired unit in March 2010 which is the first supercritical unit in Latin America. This supercritical boiler was designed with state of the art technologies such as low NOx burners, high fineness pulverizers, advanced vertical furnace wall technology and so on. Especially the advanced vertical furnace wall technology with some improvements is a key technology to realize swift load changes such as 5% load per minute ramping rate with assuring dynamic characteristics. Recently the requirement of the high efficiency and the swift load changes for the power boilers has been increased so that even a coal-fired unit needs flexible operation characteristics for balancing variety of power sources. One of the challenges for the swift load change is to keep the furnace wall metal temperature low during the load change, which the advanced vertical furnace wall could realize. The report describes the features of the unit and commissioning result including load swing test results in details.

  18. Distribution of trace elements in selected pulverized coals as a function of particle size and density

    Science.gov (United States)

    Senior, C.L.; Zeng, T.; Che, J.; Ames, M.R.; Sarofim, A.F.; Olmez, I.; Huggins, Frank E.; Shah, N.; Huffman, G.P.; Kolker, A.; Mroczkowski, S.; Palmer, C.; Finkelman, R.

    2000-01-01

    Trace elements in coal have diverse modes of occurrence that will greatly influence their behavior in many coal utilization processes. Mode of occurrence is important in determining the partitioning during coal cleaning by conventional processes, the susceptibility to oxidation upon exposure to air, as well as the changes in physical properties upon heating. In this study, three complementary methods were used to determine the concentrations and chemical states of trace elements in pulverized samples of four US coals: Pittsburgh, Illinois No. 6, Elkhorn and Hazard, and Wyodak coals. Neutron Activation Analysis (NAA) was used to measure the absolute concentration of elements in the parent coals and in the size- and density-fractionated samples. Chemical leaching and X-ray absorption fine structure (XAFS) spectroscopy were used to provide information on the form of occurrence of an element in the parent coals. The composition differences between size-segregated coal samples of different density mainly reflect the large density difference between minerals, especially pyrite, and the organic portion of the coal. The heavy density fractions are therefore enriched in pyrite and the elements associated with pyrite, as also shown by the leaching and XAFS methods. Nearly all the As is associated with pyrite in the three bituminous coals studied. The sub-bituminous coal has a very low content of pyrite and arsenic; in this coal arsenic appears to be primarily organically associated. Selenium is mainly associated with pyrite in the bituminous coal samples. In two bituminous coal samples, zinc is mostly in the form of ZnS or associated with pyrite, whereas it appears to be associated with other minerals in the other two coals. Zinc is also the only trace element studied that is significantly more concentrated in the smaller (45 to 63 ??m) coal particles.

  19. Gasification in pulverized coal flames. Final report (Part I). Pulverized coal combustion and gasification in a cyclone reactor: experiment and model

    Energy Technology Data Exchange (ETDEWEB)

    Barnhart, J. S.; Laurendeau, N. M.

    1979-05-01

    A unified experimental and analytical study of pulverized coal combustion and low-BTU gasification in an atmospheric cyclone reactor was performed. Experimental results include several series of coal combustion tests and a coal gasification test carried out via fuel-rich combustion without steam addition. Reactor stability was excellent over a range of equivalence ratios from .67 to 2.4 and air flowrates from 60 to 220 lb/hr. Typical carbon efficiencies were 95% for air-rich and stoichiometric tests and 80% for gasification tests. The best gasification results were achieved at an equivalence ratio of 2.0, where the carbon, cold gas and hot gas efficiencies were 83, 45 and 75%, respectively. The corresponding product gas heating value was 70 BTU/scf. A macroscopic model of coal combustion in the cyclone has been developed. Fuel-rich gasification can also be modeled through a gas-phase equilibrium treatment. Fluid mechanics are modeled by a particle force balance and a series combination of a perfectly stirred reactor and a plug flow reactor. Kinetic treatments of coal pyrolysis, char oxidation and carbon monoxide oxidation are included. Gas composition and temperature are checked against equilibrium values. The model predicts carbon efficiency, gas composition and temperature and reactor heat loss; gasification parameters, such as cold and hot gas efficiency and make gas heating value, are calculated for fuel-rich conditions. Good agreement exists between experiment and theory for conditions of this investigation.

  20. Biomass and waste gasification in pulverised coal-fired boilers

    Energy Technology Data Exchange (ETDEWEB)

    Nieminen, M.; Kurkela, E.; Palonen, J. [VTT Processes, Espoo (Finland)

    2004-07-01

    The replacement of coal in existing large pulverised coal-fired boilers is a cost-effective way to lower the CO{sub 2} emissions of power production. A power plant concept consisting of a gasifier connected to a large conventional boiler with a high efficiency steam cycle offers an attractive and efficient way house local biomass and waste sources in energy production. In the simplified concept clean biomass or waste is gasifier and gas is directly fed to PC boiler and co-combusted with coal. At Kymijarvi power plant in Lahti, Finland, 60 MW circulating fluidized bed gasifier was commissioned in early 1998 and has since then been in commercial operation replacing hard coal in a 360 MW{sub th} boiler producing power and district heat. The annual gasifier availability has been over 95% in each year and the Lahti plant has clearly demonstrated that the technology is technically proven and is able to reduce the emission of CO{sub 2}, SO{sub 2}, dust and NOx compared to coal-alone combustion. Contaminated biomass or waste fuels can also be utilised for replacing coal in large-scale PC boiler but most of the harmful contaminants have to be removed prior co-combustion of the gas. Product gas cleaning makes it possible to utilise even fuels with higher chlorine and metal contents. The dry gas cleaning methods have been tested at pilot scale and will be soon demonstrated in gasification plants designed for solid recovered fuels originating form household and industrial wastes. 5 refs., 4 figs., 5 tabs.

  1. Slagging characteristics of molten coal ash on silicon-aluminum combustion liners of boiler

    Institute of Scientific and Technical Information of China (English)

    2008-01-01

    In order to study the slagging characteristics of boiler combustion liners during pulverized coal stream combustion,the slag samples on the surface of combustion liner were investigated by X-ray diffractometry,scan electron microscopy and energy dispersive X-ray analysis,and the transformation characteristics of the compositions and crystal phases were studied.The results show that the size of slag granules decreases as the slagging temperature increases;the crystallinity of coal ash I reduces to about 48.6% when the temperature is increased up to 1 350 ℃,and that of the coal ash Ⅱ reduces to about 65% when the temperature is increased up to 1 500 ℃;the encroachment of molten coal ash to the combustion liner is strengthened.At the same time,the diffusion and the segregation of the compositions in combustion liners have selectivity,which is in favor of enhancing the content of crystal phases,weakening the conglutination among molten slag compositions and combustion liner,and avoiding yielding big clinkers.But the diffusion of the compositions in combustion liners increases the porosity and decreases the mechanical intensity of combustion liner,and makes the slag encroachment to the liner become more serious.

  2. Economics of fuel alternatives - oil, coal and bark boilers

    Energy Technology Data Exchange (ETDEWEB)

    Knight, W.E.; Jansen, B.M.; May, J.C.

    1984-07-01

    A method for comparing the relative economics of burning oil, bark or wastewood, and coal to generate steam is illustrated through several case plans. It was assumed that a 150,000-lb/h (68 ton/h) boiler will generate 600-psig (4134-kPa), 700 degrees F (371 degrees C) steam, that it will be added to an existing steam generating plant, and that it will be connected to the existing main steam header and to the boiler feedwater discharge header. The scope of new construction is therefore limited to the following equipment and their related structures: boiler, fuel handling, combustion controls, burner, safety system, draft fans, particulate collection, ash handling, stack, foundations. Plans involving bark, wastewood, and coal fuels are based on the assumptions that the plant has

  3. Technical notes for the conceptual design for an atmospheric fluidized-bed direct combustion power generating plant. [Comparison of AFB plant and pulverized coal plant

    Energy Technology Data Exchange (ETDEWEB)

    None

    1978-04-01

    The first part of this report presents a comparison of the conceptual designs of a large (570 MW(e)) pulverized coal (PC) steam generator equipped with a wet limestone flue gas desulfurization (FGD) system and two equivalent sized atmospheric fluidized bed (AFB) steam generators including balance of plants for electric-power generation. The reader is cautioned that this portion of the report compares a zero generation AFB technology to pulverized coal technology which has been operationally and economically optimized for the past half-century. This comparison is intended to be indicative of whether further development of the AFB concept as a viable alternative to the PC/FGD concept for electric-power generation is merited. In the second part, the load-following capability of a once-through subcritical atmospheric fluidized bed boiler is analyzed. Digital computer simulation predictions of the plant's response to open loop step changes in firing rate, feedwater flow, governor valve, unit load demand, etc, are made. The predicted response of throttle pressure, steam temperature, unit load, etc, are compared to the response of a conventional coal-fired, once-through, subcritical unit. The load-following capability is assessed through this qualitative comparison. Additional model response predictions are also presented for which no test data are presently available.

  4. A burner for plasma-coal starting of a boiler

    Science.gov (United States)

    Peregudov, V. S.

    2008-04-01

    Advanced schemes of a plasma-coal burner with single-and two-stage chambers for thermochemical preparation of fuel are described. The factors causing it becoming contaminated with slag during oil-free starting of a boiler are considered, and methods for preventing this phenomenon are pointed out.

  5. A burner for plasma-coal starting of a boiler

    Energy Technology Data Exchange (ETDEWEB)

    V.S. Peregudov [Kutateladze Institute of Thermal Physics, Siberian Branch of the Russian Academy of Sciences, Novosibirsk (Russian Federation)

    2008-04-15

    Advanced schemes of a plasma-coal burner with single-and two-stage chambers for thermochemical preparation of fuel are described. The factors causing it becoming contaminated with slag during oil-free starting of a boiler are considered, and methods for preventing this phenomenon are pointed out.

  6. Practice of promoting pulverized coal injection rate at no.4 blast furnace of China Steel Corporation

    Energy Technology Data Exchange (ETDEWEB)

    Liang, N.W.; Chang, C.T [China Steel Corp., Kaohsiung, Taiwan (China)

    2008-07-01

    In 2006, the China Steel Corporation (CSC) upgraded the injection system of its no.4 blast furnace to increase the pulverized coal (PC) rate which averaged 136 to 143 kg/thm. This paper described the scheduled shutdown of the furnace in May 2007 in order to modify it from a dilute phase injection system to a dense phase system using the technology of the Kuettner Company. Through proper burden distribution and operational parameter adjustments, the pulverized coal (PC) rate was increased to 178 kg/thm by November 2007, corresponding to a 65 t/hr injection rate with a productivity of 2.58 t/m{sup 3}/d. This paper described the challenges encountered following commissioning as well as the strategies of process control. The main differences between the existing and new injection system were that nitrogen was used to substitute compressed air as the conveying gas and the coal to gas ratio was increased from about 10 to 30 kg/kg. As a result, the transport method and the operation pressure had to be reassessed. This paper described the coal blend injection; screening facility for coal preparation; location of the distributor; and coal accumulation in the coal flow meter. The blast furnace adjustments included burden thickness control; burden distribution adjustment; improvement of raw material quality; and theoretical flame temperature adjustment. The upgrade project has proven to be very successful and has improved the competitiveness of CSC blast furnace no.4 significantly. Plans to upgrade the no.2 and no.3 blast furnaces are underway. Once completed, the operating cost and coke consumption of the blast furnaces will be reduced considerably. The modification to dense phase conveying system has shown that coal with high Hardgrove Index requires a higher driving force in the pneumatic dense phase transport and that coal mill equipped with a rotating classifier is recommended along with screens at the upstream of the feed tank. 3 refs., 6 tabs., 9 figs.

  7. DETERMINATION OF GRANULOMETRIC COMPOSITION OF PULVERIZED COAL BY AUTOMATED SYSTEM

    Directory of Open Access Journals (Sweden)

    A. S. Chernenko

    2015-01-01

    Full Text Available The method of granulometric composition determination of dry powders by a shadow method in the automated system of determination of quantitative structure is described. The granulometric analysis of coal-dust fuel particles is carried out. Comparison with results of digital microscopy allowed to establish a variety of used method advantages.

  8. Novel fragmentation model for pulverized coal particles gasification in low temperature air thermal plasma

    Directory of Open Access Journals (Sweden)

    Jovanović Rastko D.

    2016-01-01

    Full Text Available New system for start-up and flame support based on coal gasification by low temperature air thermal plasma is planned to supplement current heavy oil system in Serbian thermal power plants in order to decrease air pollutions emission and operational costs. Locally introduced plasma thermal energy heats up and ignites entrained coal particles, thus starting chain process which releases heat energy from gasified coal particles inside burner channel. Important stages during particle combustion, such as particle devolatilisation and char combustion, are described with satisfying accuracy in existing commercial CFD codes that are extensively used as powerful tool for pulverized coal combustion and gasification modeling. However, during plasma coal gasification, high plasma temperature induces strong thermal stresses inside interacting coal particles. These stresses lead to “thermal shock” and extensive particle fragmentation during which coal particles with initial size of 50-100 m disintegrate into fragments of at most 5-10 m. This intensifies volatile release by a factor 3-4 and substantially accelerates the oxidation of combustible matter. Particle fragmentation, due to its small size and thus limited influence on combustion process is commonly neglected in modelling. The main focus of this work is to suggest novel approach to pulverized coal gasification under high temperature conditions and to implement it into commercial comprehensive code ANSYS FLUENT 14.0. Proposed model was validated against experimental data obtained in newly built pilot scale D.C plasma burner test facility. Newly developed model showed very good agreement with experimental results with relative error less than 10%, while the standard built-in gasification model had error up to 25%.

  9. Increase of Ecological Safety, Reliability and Efficiency of Coal-Fired Boilers

    Directory of Open Access Journals (Sweden)

    Volkov E.P.

    2017-04-01

    Full Text Available The changes of environmental legislation of the Russian Federation will lead to a drastic increase of the ecological payments for environmental pollution in excess of technological standards. Significant excess in relative emissions of nitrogen oxides take place in burning solid fuel with liquid slag-tap removal. The purpose of this article was to develop technical solutions for low-cost reconstruction of the boilers to ensure efficient combustion of the fuel and technological standards of emissions of nitrogen oxides. As shown the use of straight-flow burners with compulsory optimization of the aerodynamics of the furnace and the organization of staged combustion of fuel will provide low nitrogen oxide emissions and efficient fuel combustion. Research on physical models has demonstrated the feasibility of increasing the angle of the pulverized coal burners down to 65-70o, and also achieved a more uniform distribution and increase the speed of the jets coming from upper and lower tertiary air vertical compartments of nozzles through the installation of the vertical extra sheets, which guide the flow in a space between jets. The results obtained allow the transfer of existing boilers with slag-tag removal to a solid with the installation of direct-flow burners and optimization of the aerodynamics of the furnace, which provides regulations for energy efficiency and ecological safety corresponding to the best, achieved technologies, and dramatically reduces environmental payments. The proposed technology in boiler BKZ-210-140F allowed reducing emissions of nitrogen oxides by more than 2 times when burning highly reactive Kuznetsk coal, as shown as an example.

  10. The past, present and future of pulverized coal injection at ThyssenKrupp Steel AG

    Energy Technology Data Exchange (ETDEWEB)

    Peters, M.; Korthas, B.; Schmole, P. [ThyssenKrupp Steel AG., Duisburg (Germany). Hot Metal Production-Metallurgy Division

    2008-07-01

    Coal injection has been used to optimize blast furnace operation at the ThyssenKrupp Steel (TKS) plants in Germany for over 25 years. The main TKS plants are located at Duisburg on the Rhine river with optimum logistical conditions for raw materials and finished products. This presentation described the long history of blast furnace operation at TKS and the optimization of the combustion process in the raceway. The key factors for controlling coal combustion were coal properties; lance design; partial pressure of oxygen in the raceway; amount of nitrogen for the pneumatic coal transport; and additives to the coal. When changing over from the all-coke to the pulverized coal (PC)-coke mode of operation, the main attention was directed to blast velocity and burden distribution. Initially, 2 injection systems were developed in 1982 for a blast furnace pilot facility in Hamborn where coal was injected through 3 tuyeres of the blast furnace. The experience gained at the pilot facility was used for other production facilities. They were evaluated in terms of plant wear, pneumatic conveying characteristics, and behaviour of the system when using different types of coal. In 1987, the Schwelgern blast furnace was equipped with the dense flow system and the blast furnace in Ruhrort was equipped with an entrained flow system and metering valves. In February 1991, blast furnace no. 9 in Hamborn was equipped with the dense flow for all 28 tuyeres and is designed for an injection rate of 250 kg/THM. 21 figs.

  11. Detailed model for practical pulverized coal furnaces and gasifiers

    Energy Technology Data Exchange (ETDEWEB)

    Smith, P.J.; Smoot, L.D.

    1989-08-01

    This study has been supported by a consortium of nine industrial and governmental sponsors. Work was initiated on May 1, 1985 and completed August 31, 1989. The central objective of this work was to develop, evaluate and apply a practical combustion model for utility boilers, industrial furnaces and gasifiers. Key accomplishments have included: Development of an advanced first-generation, computer model for combustion in three dimensional furnaces; development of a new first generation fouling and slagging submodel; detailed evaluation of an existing NO{sub x} submodel; development and evaluation of an improved radiation submodel; preparation and distribution of a three-volume final report: (a) Volume 1: General Technical Report; (b) Volume 2: PCGC-3 User's Manual; (c) Volume 3: Data Book for Evaluation of Three-Dimensional Combustion Models; and organization of a user's workshop on the three-dimensional code. The furnace computer model developed under this study requires further development before it can be applied generally to all applications; however, it can be used now by specialists for many specific applications, including non-combusting systems and combusting geseous systems. A new combustion center was organized and work was initiated to continue the important research effort initiated by this study. 212 refs., 72 figs., 38 tabs.

  12. Detailed model for practical pulverized coal furnaces and gasifiers

    Energy Technology Data Exchange (ETDEWEB)

    Smith, P.J.; Smoot, L.D.

    1989-08-01

    This study has been supported by a consortium of nine industrial and governmental sponsors. Work was initiated on May 1, 1985 and completed August 31, 1989. The central objective of this work was to develop, evaluate and apply a practical combustion model for utility boilers, industrial furnaces and gasifiers. Key accomplishments have included: Development of an advanced first-generation, computer model for combustion in three dimensional furnaces; development of a new first generation fouling and slagging submodel; detailed evaluation of an existing NO{sub x} submodel; development and evaluation of an improved radiation submodel; preparation and distribution of a three-volume final report: (a) Volume 1: General Technical Report; (b) Volume 2: PCGC-3 User's Manual; (c) Volume 3: Data Book for Evaluation of Three-Dimensional Combustion Models; and organization of a user's workshop on the three-dimensional code. The furnace computer model developed under this study requires further development before it can be applied generally to all applications; however, it can be used now by specialists for many specific applications, including non-combusting systems and combusting geseous systems. A new combustion center was organized and work was initiated to continue the important research effort initiated by this study. 212 refs., 72 figs., 38 tabs.

  13. Analysis of Pulverized Coal by Laser-Induced Breakdown Spectroscopy

    Institute of Scientific and Technical Information of China (English)

    2005-01-01

    Laser-induced breakdown spectroscopy (LIBS) has been used to detect atomic species in various environments. The quantitative analysis (C, H, O, N and S) of representative coal samples are being carried out with LIBS, and the effects of particle size are analyzed.A powerful pulse Nd:YAG laser is focused on the coal sample at atmosphere pressure, and the emission spectra from laser-induced plasmas are measured by time-resolved spectroscopy, and the intensity of analyzed spectral lines is obtained through observing the laser plasma with a delay time of 0.4μs. The experimental results show that the slope of calibration curve is nearly 1 when the concentration of the analyzed element is relatively low, and the slope of curve is nearly 0.5 when the concentration of C is higher than other elements. In addition, using the calibration-free model without self-absorption effect, the results show that the decreasing of particle size leads to an increase of the plasma temperature.

  14. 煤质变化对Shell粉煤气化工艺的影响%THE EFFECT OF COAL QUALITY CHANGE ON SHELL PULVERIZED-COAL GASIFICATION PROCESS

    Institute of Scientific and Technical Information of China (English)

    吴国祥

    2011-01-01

    The Shell pulverized-coal gasification process is introduced,the specific requirement for coal quality by Shell pulverized-coal gasification process summarized,several factors related to coal quality and the effect of the changes of these factors on Shell pulverized-coal gasification plant highlighted and the preventive measures based on the effects concluded.%介绍Shell粉煤气化工艺流程,总结Shell粉煤气化工艺对煤质的具体要求,阐述与煤质相关的几方面因素及这些因素的变化对Shell粉煤气化装置的影响,并根据这些影响得出相应的预防措施。

  15. Boiler Briquette Coal versus Raw Coal: Part II-Energy, Greenhouse Gas, and Air Quality Implications.

    Science.gov (United States)

    Zhang, Junfeng; Ge, Su; Bai, Zhipeng

    2001-04-01

    The objective of this paper is to conduct an integrated analysis of the energy, greenhouse gas, and air quality impacts of a new type of boiler briquette coal (BB-coal) in contrast to those of the raw coal from which the BB-coal was formulated (R-coal). The analysis is based on the source emissions data and other relevant data collected in the present study and employs approaches including the construction of carbon, energy, and sulfur balances. The results show that replacing R-coal with BB-coal as the fuel for boilers such as the one tested would have multiple benefits, including a 37% increase in boiler thermal efficiency, a 25% reduction in fuel demand, a 26% reduction in CO2 emission, a 17% reduction in CO emission, a 63% reduction in SO2 emission, a 97% reduction in fly ash and fly ash carbon emission, a 22% reduction in PM2.5 mass emission, and a 30% reduction in total emission of five toxic hazardous air pollutant (HAP) metals contained in PM10. These benefits can be achieved with no changes in boiler hardware and with a relatively small amount of tradeoffs: a 30% increase in PM10 mass emission and a 9-16% increase in fuel cost.

  16. Boiler briquette coal versus raw coal: Part II--Energy, greenhouse gas, and air quality implications.

    Science.gov (United States)

    Zhang, J; Ge, S; Bai, Z

    2001-04-01

    The objective of this paper is to conduct an integrated analysis of the energy, greenhouse gas, and air quality impacts of a new type of boiler briquette coal (BB-coal) in contrast to those of the raw coal from which the BB-coal was formulated (R-coal). The analysis is based on the source emissions data and other relevant data collected in the present study and employs approaches including the construction of carbon, energy, and sulfur balances. The results show that replacing R-coal with BB-coal as the fuel for boilers such as the one tested would have multiple benefits, including a 37% increase in boiler thermal efficiency, a 25% reduction in fuel demand, a 26% reduction in CO2 emission, a 17% reduction in CO emission, a 63% reduction in SO2 emission, a 97% reduction in fly ash and fly ash carbon emission, a 22% reduction in PM2.5 mass emission, and a 30% reduction in total emission of five toxic hazardous air pollutant (HAP) metals contained in PM10. These benefits can be achieved with no changes in boiler hardware and with a relatively small amount of tradeoffs: a 30% increase in PM10 mass emission and a 9-16% increase in fuel cost.

  17. Effects of pulverized coal fly-ash addition as a wet-end filler in papermaking

    Energy Technology Data Exchange (ETDEWEB)

    Sinha, A.S.K. [SLIET, Longowal (India). Dept. of Chemical Technology

    2008-09-15

    This experimental study is based on the innovative idea of using pulverized coal fly ash as a wet-end filler in papermaking. This is the first evaluation of the possible use of fly ash in the paper industry. Coal-based thermal power plants throughout the world are generating fly ash as a solid waste product. The constituents of fly ash can be used effectively in papermaking. Fly ash has a wide variation in particle size, which ranges from a few micrometers to one hundred micrometers. Fly ash acts as an inert material in acidic, neutral, and alkaline papermaking processes. Its physical properties such as bulk density (800-980 kg/m{sup 3}), porosity (45%-57%), and surface area (0.138-2.3076 m{sup 2}/g) make it suitable for use as a paper filler. Fly ash obtained from thermal power plants using pulverized coal was fractionated by a vibratory-sieve stack. The fine fraction with a particle size below 38 micrometers was used to study its effect on the important mechanical-strength and optical properties of paper. The effects of fly-ash addition on these properties were compared with those of kaolin clay. Paper opacity was found to be much higher with fly ash as a filler, whereas brightness decreased as the filler percentage increased Mechanical strength properties of the paper samples with fly ash as filler were superior to those with kaolin clay.

  18. Hot Corrosion Studies in Coal Fired Boiler Environment

    Directory of Open Access Journals (Sweden)

    Kamal Subhash

    2014-07-01

    Full Text Available Hot corrosion behaviour of the bare and D-gun coated superfer 800H exposed to low temperature super-heater zone of the coal fired boiler of Guru Nanak Dev Thermal Power Plant, Bathinda, Punjab, India. The specimens were hanged in the platen super-heater of coal fired boiler where the gas temperature was around 900 °C ±10 °C. Hot corrosion experiments were performed for 10 cycles, each cycle consisting of 100 hours exposure followed by 1 hour cooling at ambient temperature. Weight change measurements were done at the end of each cycle. The weight change data used for predicting hot corrosion behaviour of the coated alloys after the total exposure of 1000 hours. The different phases and their distribution in the hot corroded specimens were analysed with the help of FE-SEM/EDS and X-ray mapping.

  19. Formation of NOx precursors during Chinese pulverized coal pyrolysis in an arc plasma jet

    Energy Technology Data Exchange (ETDEWEB)

    Wei-ren Bao; Jin-cao Zhang; Fan Li; Li-ping Chang [Taiyuan University of Technology, Taiyuan (China). Key Laboratory of Coal Science and Technology

    2007-08-15

    The formation of NOx precursors (HCN and NH{sub 3}) from the pyrolysis of several Chinese pulverized coals in an arc plasma jet was investigated through both thermodynamic analysis of the C-H-O-N system and experiments. Results of thermodynamic analysis show that the dominant N-containing gaseous species is HCN together with a small amount of ammonia above the temperature of 2000 K. The increase of H content advances the formation of HCN and NH{sub 3}, but the yields of HCN and NH{sub 3} are decreased with a high concentration of O in the system. These results are accordant with the experimental data. The increasing of input power promotes the formation of HCN and NH{sub 3} from coal pyrolysis in an arc plasma jet. Tar-N is not formed during the process. The yield of HCN changes insignificantly with the changing of the residence time of coal particles in the reactor, but that of NH{sub 3} decreases as residence times increase because of the relative instability at high temperature. Adsorption and gasification of CO{sub 2} on the coal surface also can restrain the formation of HCN and NH{sub 3} compare to the results in an Ar plasma jet. Yields of HCN and NH{sub 3} are sensitive to the coal feeding rate, indicating that NOx precursors could interact with the nascent char to form other N-containing species. The formation of HCN and NH{sub 3} during coal pyrolysis in a H{sub 2}/Ar plasma jet are not dependent on coal rank. The N-containing gaseous species is released faster than others in the volatiles during coal pyrolysis in an arc plasma jet, and the final nitrogen content in the char is lower than that in the parent coal, which it is independent of coal type. 16 refs., 9 figs., 1 tab.

  20. Flat-flame burner studies of pulverized-coal combustion. Experimental results on char reactivity

    Energy Technology Data Exchange (ETDEWEB)

    Peck, R.E.; Shi, L.

    1996-12-01

    Structure of laminar, premixed pulverized-coal flames in a 1-D reactor has been studied with emphasis on char reactivity. A 1.1-meter-long tube furnace accommodated high-temperature environments and long residence times for the laminar flames produced by a flat-flame, coal-dust burner. Experiments were conducted at different operating conditions (fuel type/size, fuel-air ratio). Measurements included solid sample composition, major gas species and hydrocarbon species concentrations, and gas- and particle-phase line-of-sight temperatures at different axial locations in flames. Degree of char burnout increased with coal volatiles content and decreased with coal particle size. Combustion in furnace was in oxidizer-deficient environment and higher burnout was achieved as the fuel-air ratio neared stoichiometric. For 0-45 {mu}m particles most of the fixed carbon mass loss occurred within 5 cm of the furnace inlet, and char reaction was slow downstream due to low oxidizer concentrations. Fixed carbon consumption of the 45-90 {mu}m particles generally was slower than for the small particles. About 40%-80% of the fixed carbon was oxidized in the furnace. Primary volatiles mass loss occurred within the first 4.5 cm, and more than 90% of the volatiles were consumed in the flames. The flames stabilized in the furnace produced less CH{sub 4} and H{sub 2} in the burnt gas than similar unconfined flames. NO concentrations were found to decrease along the furnace and to increase with decreasing fuel/air ratio. Temperature measurement results showed that gas-phase temperatures were higher than solid-phase temperatures. Temperatures generally decreased with decreasing volatiles content and increased as the equivalence ratio approached one. The results can be used to interpret thermochemical processes occurring in pulverized-coal combustion. (au) 15 refs.

  1. Physicochemical properties and potential health effects of nanoparticles from pulverized coal combustion

    Institute of Scientific and Technical Information of China (English)

    YU DunXi; XU MingHou; YAO Hong; LIU XiaoWei; ZHOU Ke; WEN Chang; LI Lin

    2009-01-01

    Nanoparticles are thought to induce more severe health impacts than larger particles. The nanoparti-cles from coal-fired boilers are classified into three size fractions with a 13-stage low pressure impactor. Their physicochemical properties are characterized by the high-resolution field emission scanning electron microscope and X-ray fluorescence spectrometer (XRF). The results show that coal-derived nanoparticles mainly consist of individual primary particles of 20-150 nm and their aggregates. Inor-ganic nanoparticles primarily contain ash-forming elements and their aggregates have a dense struc-ture. Organic nanoparticles are dominated by the element carbon and their aggregates have a loose structure. Nanoparticles from the same boiler have a similar composition and are primarily composed of sulfur, refractory elements and alkali/alkaline elements. Some transition and heavy metals are also detected. For different boilers, greater differences are observed in the production of the nanoparticles and their composition, possibly due to the use of low-NOx burners. Coal-derived nanoparticles have a small size, large specific surface area and complicated chemical composition, and thus are potentially more harmful to human health.

  2. Computational Fluid Dynamics (CFD) Modeling for High Rate Pulverized Coal Injection (PCI) into the Blast Furnace

    Energy Technology Data Exchange (ETDEWEB)

    Dr. Chenn Zhou

    2008-10-15

    Pulverized coal injection (PCI) into the blast furnace (BF) has been recognized as an effective way to decrease the coke and total energy consumption along with minimization of environmental impacts. However, increasing the amount of coal injected into the BF is currently limited by the lack of knowledge of some issues related to the process. It is therefore important to understand the complex physical and chemical phenomena in the PCI process. Due to the difficulty in attaining trus BF measurements, Computational fluid dynamics (CFD) modeling has been identified as a useful technology to provide such knowledge. CFD simulation is powerful for providing detailed information on flow properties and performing parametric studies for process design and optimization. In this project, comprehensive 3-D CFD models have been developed to simulate the PCI process under actual furnace conditions. These models provide raceway size and flow property distributions. The results have provided guidance for optimizing the PCI process.

  3. Comparative study of semi-industrial-scale flames of pulverized coals and biomass

    Energy Technology Data Exchange (ETDEWEB)

    Ballester, J.; Barroso, J.; Cerecedo, L.M.; Ichaso, R. [University of Zaragoza, Zaragoza (Spain)

    2005-05-01

    Three p.f. flames have been studied in a semi-industrial furnace, using different fuels: a bituminous coal, a lignite, and a biomass (oak sawdust). The operating conditions were exactly the same for the two coals, and very similar to those for the biornass flame. The objective was to evaluate the impact of differences in fuel composition on flame characteristics, through measurement of the spatial distribution of the main parameters: temperature and concentrations of O{sub 2}, CO, NOx, unburnt hydrocarbons, and N{sub 2}O. The higher volatiles content in the lignite leads to higher temperatures and more intense combustion than the bituminous coal. Nevertheless, as might be expected, more marked differences are observed between the flames from the biomass and coals. The much higher volatiles content of the wood results in a more intense flame close to the burner, as indicated by visual observations and by concentrations of unburnt gases (CO and unburnt hydrocarbons) in that zone. It is remarkable that the combustion zone extends further for the biomass; while unburnt species were very low for the coals at an axial distance of 1 m, high values were detected for the pulverized oak. The measurements suggest that two stages can be distinguished in the biomass flame: a zone of intense combustion close to the burner, followed by a second region where the large biomass particles gradually devolatilize and are consumed.

  4. Combustion characteristics of pulverized coal and air/gas premixed flame in a double swirl combustor

    Energy Technology Data Exchange (ETDEWEB)

    Kamal, M.M. [Ain Shams University, Cairo (Egypt). Faculty of Education

    2009-07-01

    An experimental work was performed to investigate the co-firing of pulverized coal and premixed gas/air streams in a double swirl combustor. The results showed that the NOx emissions are affected by the relative rates of thermal NOx formation and destruction via the pyrolysis of the fuel-N species in high temperature fuel-rich zones. Various burner designs were tested in order to vary the temperature history and the residence time across both coal and gas flames inside the furnace. It was found that by injecting the coal with a gas/air mixture as a combined central jet surrounded by a swirled air stream, a double flame envelope develops with high temperature fuel-rich conditions in between the two reaction zones such that the pyrolysis reactions to N{sub 2} are accelerated. A further reduction in the minimum NOx emissions, as well as in the minimum CO concentrations, was reported for the case where the coal particles are fed with the gas/air mixture in the region between the two swirled air streams. On the other hand, allocating the gas/air mixture around the swirled air-coal combustion zone provides an earlier contact with air and retards the NOx reduction mechanism in such a way that the elevated temperatures around the coal particles allow higher overall NOx emissions. The downstream impingement of opposing air jets was found more efficient than the impinging of particle non-laden premixed flames for effective NOx reduction. In both cases, there is an upstream flow from the stagnation region to the coal primary combustion region, but with the case of air impingement, the hot fuel-rich zone develops earlier. The optimum configuration was found by impinging all jets of air and coal-gas/air mixtures that pronounced minimum NOx and CO concentrations of 310 and 480ppm, respectively.

  5. Application and Operational Maintenance Experience of Plasma Pulverized Coal Ignition Combustion Technology%等离子煤粉点火燃烧技术的应用及运维经验

    Institute of Scientific and Technical Information of China (English)

    刘俊臻

    2012-01-01

    介绍了交流等离子煤粉点火系统的工作原理、点火燃烧器功能、点火燃烧机理以及在上海吴泾热电厂2台1125t/h锅炉上的应用情况。总结了等离子煤粉点火装置和稳燃系统的安装、调试与日常运维经验。实践表明,等离子煤粉点火技术是一种节能、环保、快速升负荷的技术。锅炉点火燃油零消耗,既提高了煤粉燃烧的经济性,又减少了燃煤电厂的烟尘排放;既改善了厂区周边环境,又降低了生产成本。交流等离子煤粉点火系统的应用,可以获得较好的经济及社会效益。%The essay introduces operational principle of alternating plasma pulverized coal ignition system, the function of ignition burner, mechanization of ignition combustion and the application of plasma pulverized coal ignition combustion technology on two 1 125 t/h boilers in Shanghai Wujing Thermal Power Plant. It also makes a summary of installation, debugging and routine operational maintenance experience for plasma pulverized coal ignition device and stabilized combustion system. The practice proves that plasma pulverized coal ignition technology is a new technology with conservation of energy, environmental protection and quick power increasing. With ignition fuel oil zero consumption, it not only raises economical efficiency of pulverized coal burning, but also reduces smoke dust discharging in coal fired power plant, and improves power plant's surroundings as well as lowers the production cost effectively. The application of alternating plasma pulverized coal ignition system brings better economic and social benefits.

  6. Estimation of Moisture Content in Coal in Coal Mills

    DEFF Research Database (Denmark)

    Odgaard, Peter Fogh; Mataji, Babak

    2006-01-01

    the moisture content of the coal is proposed based on a simple dynamic energy model of a coal mill, which pulverizes and dries the coal before it is burned in the boiler. An optimal unknown input observer is designed to estimate the moisture content based on an energy balance model. The designed moisture...

  7. Estimation of Moisture Content in Coal in Coal Mills

    DEFF Research Database (Denmark)

    Odgaard, Peter Fogh; Mataji, B.

    the moisture content of the coal is proposed based on a simple dynamic energy model of a coal mill, which pulverizes and dries the coal before it is burned in the boiler. An optimal unknown input observer is designed to estimate the moisture content based on an energy balance model. The designed moisture...

  8. Partitioning behavior of trace elements during pilot-scale combustion of pulverized coal and coal-water slurry fuel

    Science.gov (United States)

    Nodelman; Pisupati; Miller; Scaroni

    2000-05-29

    Release pathways for inorganic hazardous air pollutants (IHAPs) from a pilot-scale, down-fired combustor (DFC) when firing pulverized coal (PC) and coal-water slurry fuel (CWSF) were identified and quantified to demonstrate the effect of fuel form on IHAP partitioning, enrichment and emissions. The baghouse capturing efficiency for each element was calculated to determine the effectiveness of IHAP emission control. Most of the IHAPs were enriched in the fly ash and depleted in the bottom ash. Mercury was found to be enriched in the flue gas, and preferentially emitted in the vapor phase. When firing CWSF, more IHAPs were partitioned in the bottom ash than when firing PC. Significant reduction of Hg emissions during CWSF combustion was also observed.

  9. NOx Control Options and Integration for US Coal Fired Boilers

    Energy Technology Data Exchange (ETDEWEB)

    Mike Bockelie; Marc Cremer; Kevin Davis; Martin Denison; Adel Sarofim; Connie Senior; Hong-Shig Shim; Dave Swenson; Bob Hurt; Eric Suuberg; Eric Eddings; Kevin Whitty; Larry Baxter; Calvin Bartholomew; William Hecker

    2006-06-30

    This is the Final Report for DOE Cooperative Agreement No: DE-FC26-00NT40753. The goal of the project was to develop cost-effective analysis tools and techniques for demonstrating and evaluating low-NOx control strategies and their possible impact on boiler performance for boilers firing US coals. The Electric Power Research Institute (EPRI) provided co-funding for this program. This project included research on: (1) In furnace NOx control; (2) Impacts of combustion modifications on boiler operation; (3) Selective Catalytic Reduction (SCR) catalyst testing and (4) Ammonia adsorption/removal on fly ash. Important accomplishments were achieved in all aspects of the project. Rich Reagent Injection (RRI), an in-furnace NOx reduction strategy based on injecting urea or anhydrous ammonia into fuel rich regions in the lower furnace, was evaluated for cyclone-barrel and PC fired utility boilers. Field tests successfully demonstrated the ability of the RRI process to significantly reduce NOx emissions from a staged cyclone-fired furnace operating with overfire air. The field tests also verified the accuracy of the Computational Fluid Dynamic (CFD) modeling used to develop the RRI design and highlighted the importance of using CFD modeling to properly locate and configure the reagent injectors within the furnace. Low NOx firing conditions can adversely impact boiler operation due to increased waterwall wastage (corrosion) and increased soot production. A corrosion monitoring system that uses electrochemical noise (ECN) corrosion probes to monitor, on a real-time basis, high temperature corrosion events within the boiler was evaluated. Field tests were successfully conducted at two plants. The Ohio Coal Development Office provided financial assistance to perform the field tests. To investigate soot behavior, an advanced model to predict soot production and destruction was implemented into an existing reacting CFD modeling tool. Comparisons between experimental data collected

  10. Condensing economizers for small coal-fired boilers and furnaces

    Energy Technology Data Exchange (ETDEWEB)

    Butcher, T.A.; Litzke, W.

    1994-01-01

    Condensing economizers increase the thermal efficiency of boilers by recovering sensible and latent heat from exhaust gas. These economizers are currently being used commercially for this purpose in a wide range of applications. Performance is dependent upon application-specific factors affecting the utility of recovered heat. With the addition of a condensing economizer boiler efficiency improvements up to 10% are possible. Condensing economizers can also capture flue gas particulates. In this work, the potential use of condensing economizers for both efficiency improvement and control of particulate emissions from small, coal water slurry-fired boilers was evaluated. Analysis was done to predict heat transfer and particulate capture by mechanisms including: inertial impaction, interception, diffusion, thermophoretic forces, and condensation growth. Shell-and-tube geometries were considered with flue gas on the outside of Teflon-covered tubes. Experimental studies were done with both air- and water-cooled economizers refit to a small boiler. Two experimental arrangements were used including oil-firing with injection of flyash upstream of the economizer and direct coal water slurry firing. Firing rates ranged from 27 to 82 kW (92,000 to 280,000 Btu/hr). Inertial impaction was found to be the most important particulate capture mechanism and removal efficiencies to 95% were achieved. With the addition of water sprays directly on the first row of tubes, removal efficiencies increased to 98%. Use of these sprays adversely affects heat recovery. Primary benefits of the sprays are seen to be the addition of small impaction sites and future design improvements are suggested in which such small impactors are permanently added to the highest velocity regions of the economizer. Predicted effects of these added impactors on particulate removal and pressure drop are presented.

  11. Formation of fine particles in co-combustion of coal and solid recovered fuel in a pulverized coal-fired power station

    DEFF Research Database (Denmark)

    Wu, Hao; Pedersen, Anne Juul; Glarborg, Peter

    2011-01-01

    Fine particles formed from combustion of a bituminous coal and co-combustion of coal with 7 th% (thermal percentage) solid recovered fuel (SRF) in a pulverized coal-fired power plant were sampled and characterized in this study. The particles from dedicated coal combustion and co-combustion both...... appear to be an important formation mechanism. The elemental composition of the particles from coal combustion showed that S and Ca were significantly enriched in ultrafine particles and P was also enriched considerably. However, compared with supermicron particles, the contents of Al, Si and K were...

  12. Experimental and modeling study of the effect of CH(4) and pulverized coal on selective non-catalytic reduction process.

    Science.gov (United States)

    Zhang, Yanwen; Cai, Ningsheng; Yang, Jingbiao; Xu, Bo

    2008-10-01

    The reduction of nitric oxide using ammonia combined with methane and pulverized coal additives has been studied in a drop tube furnace reactor. Simulated flue gas with 1000 ppm NO(x) and 3.4% excess oxygen was generated by cylinder gas. Experiments were performed in the temperature range of 700-1200 degrees C to investigate the effects of additives on the DeNO(x) performance. Subsequently, a kinetic mechanism was modified and validated based on experimental results, and a computational kinetic modeling with CHEMKIN was conducted to analyze the secondary pollutants. For both methane and pulverized coal additives, the temperature window is shifted towards lower temperatures. The appropriate reaction temperature is shifted to about 900 and 800 degrees C, respectively with 1000 ppm methane and 0.051 g min(-1) pulverized lignite coal. The addition of methane and pulverized coal widens the temperature window towards lower temperature suggesting a low temperature application of the process. Furthermore, selective non-catalytic reduction (SNCR) reaction rate is accelerated evidently with additives and the residence time to complete the reaction is shortened distinctly. NO(x) reduction efficiency with 80% is achieved in about 0.3s without additive at 1000 degrees C. However, it is achieved in only about 0.2s with 100 ppm methane as additive, and only 0.07 and 0.05s are needed respectively for the cases of 500 and 1000 ppm methane. The modified kinetic modeling agrees well with the experimental results and reveals additional information about the process. Investigation on the byproducts where NO(2) and N(2)O were analyzed by modeling and the others were investigated by experimental means indicates that emissions would not increase with methane and pulverized coal additions in SNCR process and the efficacious temperature range of SNCR reaction is widened approximately with 100 degrees C.

  13. Flame radiant image numeralization for pulverized coal combustion in BF raceway

    Institute of Scientific and Technical Information of China (English)

    WEN Liang-ying; OU Yang-qi; BAI Chen-guang; WANG Hua

    2005-01-01

    In order to establish correlativity between pulverized coal combustion in a blast furnace raceway and its radiant image, we investigated the relationships between two dimensional radiant images and three dimensional radiant energy in a blast furnace raceway, focusing on the correlativity of the numerical simulation of combustion processes with the connection of radiant images information and space temperature distribution. We calculated the uneven radiate characteristic parameterby taking radiant images as a kind of radiative boundary for numerical simulation of combustion processes, and put forward a method to examine three-dimensional temperatures distribution in blast furnace raceway by radiant image processing. The numeral temperature fields matching the real combustion can be got by the numeric image processing technique.

  14. Innovative clean coal technology (ICCT): demonstration of selective catalytic reduction (SCR) technology for the control of nitrogen oxide (NO{sub x}) emission from high-sulfur, coal-fired boilers - economic evaluation of commercial-scale SCR applications for utility boilers

    Energy Technology Data Exchange (ETDEWEB)

    Healy, E.C.; Maxwell, J.D.; Hinton, W.S.

    1996-09-01

    This report presents the results of an economic evaluation produced as part of the Innovative Clean Coal Technology project, which demonstrated selective catalytic reduction (SCR) technology for reduction of NO{sub x} emissions from utility boilers burning U.S. high-sulfur coal. The document includes a commercial-scale capital and O&M cost evaluation of SCR technology applied to a new facility, coal-fired boiler utilizing high-sulfur U.S. coal. The base case presented herein determines the total capital requirement, fixed and variable operating costs, and levelized costs for a new 250-MW pulverized coal utility boiler operating with a 60-percent NO{sub x} removal. Sensitivity evaluations are included to demonstrate the variation in cost due to changes in process variables and assumptions. This report also presents the results of a study completed by SCS to determine the cost and technical feasibility of retrofitting SCR technology to selected coal-fired generating units within the Southern electric system.

  15. Characterization of Oxy-combustion Impacts in Existing Coal-fired Boilers

    Energy Technology Data Exchange (ETDEWEB)

    Bradley Adams; Andrew Fry; Constance Senior; Hong Shim; Huafeng Wang; Jost Wendt; Christopher Shaddix

    2009-06-30

    This report summarizes Year 1 results of a research program designed to use multi-scale experimental studies and fundamental theoretical models to characterize and predict the impacts of retrofit of existing coal-fired utility boilers for oxy-combustion. Through the course of Year 1 activities, great progress was made toward understanding the issues associated with oxy-combustion retrofit of coal-fired boilers. All four Year 1 milestones and objectives have been, or will be, completed on schedule and within budget. Progress in the four milestone areas may be summarized as follows: • University of Utah has performed size segregated ash composition measurements in the Oxy-Fuel Combustor (OFC). These experiments indicate that oxy-combustion retrofit may impact ash aerosol mineral matter composition. Both flame temperature and flue gas composition have been observed to influence the concentration of calcium, magnesium and iron in the fine particulate. This could in turn impact boiler fouling and slagging. • Sandia National Labs has shown that char oxidation rate is dependent on particle size (for sizes between 60 and 100 microns) by performing fundamental simulations of reacting char particles. These predictions will be verified by making time-resolved optical measurements of char particle temperature, velocity and size in bench-scale experiments before the end of Year 1. • REI and Siemens have completed the design of an oxy-research burner that will be mounted on University of Utah’s pilot-scale furnace, the L1500. This burner will accommodate a wide range of O2, FGR and mixing strategies under conditions relevant for utility boiler operation. Through CFD modeling of the different burner designs, it was determined that the key factor influencing flame stabilization location is particle heat-up rate. The new oxy-research burner and associated equipment is scheduled for delivery before the end of Year 1. • REI has completed a literature survey of slagging and

  16. NOx CONTROL OPTIONS AND INTEGRATION FOR US COAL FIRED BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    Mike Bockelie; Marc Cremer; Kevin Davis; Connie Senior; Bob Hurt; Eric Eddings; Larry Baxter

    2002-04-30

    This is the seventh Quarterly Technical Report for DOE Cooperative Agreement No: DE-FC26-00NT40753. The goal of the project is to develop cost effective analysis tools and techniques for demonstrating and evaluating low NOx control strategies and their possible impact on boiler performance for firing US coals. The Electric Power Research Institute (EPRI) is providing co-funding for this program. This program contains multiple tasks and good progress is being made on all fronts. A series of field tests for RRI at the Ameren Sioux Unit No.1 have demonstrated that RRI can provide up to 30% NOx reduction over the use of over fire air in large scale (480MW) cyclone fired utility boilers. The field tests and modeling results are in good agreement. Final data analysis has been completed for tests performed at Eastlake Power Station of a real-time waterwall corrosion monitoring system. The tests demonstrated that corrosion could be measured accurately in real-time in normal boiler operations, and an assessment of waterwall wastage could be made without impacting boiler availability. Detailed measurements of soot volume fraction have been performed for a coal burner in a pilot scale test furnace. The measured values are in good agreement with the expected trends for soot generation and destruction. Catalysts from four commercial manufacturers have been ordered and one of the samples was received this quarter. Several in situ analyses of vanadium-based SCR catalyst systems were completed at BYU. Results to date indicate that the system produces results that represent improvements compared to literature examples of similar experiments. Construction of the catalyst characterization system (CCS) reactor is nearly complete, with a few remaining details discussed in this report. A literature review originally commissioned from other parties is being updated and will be made available under separate cover as part of this investigation. Fabrication of the multi-catalyst slipstream

  17. Low—NOx Combustion and Experimental Investigation in a ROtary Type Pulverized Coal Classifier

    Institute of Scientific and Technical Information of China (English)

    WenjunKong; ShangmoCheng; 等

    1995-01-01

    In order to improve the combustion conditions,maximize the carbon burnout for low-NOx firing systems and meet the requirements for ignition and flame stabilization as low volatile and low quality coal are burned in boilers,finer pulverzed coal should be used .Hence.it is of great practical importance to study the rotary type classifier for the MPS type medium-speed mill.In this pper,we first review the low-NOx combustion technology,then some model tests of rotating classifier are completed.The results show that the classifier performances are very satisfactory,with the fineness of the finished produce being R90f<10%,Rules for designing and controlling rotating classifier are also developed in this paper.

  18. Effect of the Reburning Zone Stoichiometry on the Nox Concentration at the Three-Stage Combustion of Pulverized Coal

    Directory of Open Access Journals (Sweden)

    Chernetskaya Nelya

    2016-01-01

    Full Text Available Numerical study of heat and mass transfer taking into account the combustion of coal particles in the furnace at the three-stage combustion of pulverized coal was performed. Analysis of the reburning zone stoichiometry on the concentration of nitrogen oxides at the furnace outlet was made. The values of excess air in the primary and reburning combustion zones, providing for the concentration of nitrogen oxides at the furnace outlet is not more than 350 mg/m3 and unburned carbon not more than 1 % when burning coal with a high content of nitrogen were established.

  19. Gasification in pulverized coal flames. Second quarterly progress report, October--December 1975. [Contains literature survey on vortex gasifier

    Energy Technology Data Exchange (ETDEWEB)

    Lenzer, R. C.; George, P. E.; Laurendeau, N. M.

    1976-01-01

    This project is concerned with the production of power and synthesis gases from pulverized coal via suspension gasification. A literature review concerning the vortex type gasifier has been completed and a survey concerning the confined jet gasifier is underway. Preliminary design of the vortex gasifier is nearing completion. Test cell and coal handling facilities are in the final stages of design and coal handling equipment has been received. A mass spectrometer has been ordered and a preliminary survey of high-temperature probes is complete.

  20. Influence of the gray gases number in the weighted sum of gray gases model on the radiative heat exchange calculation inside pulverized coal-fired furnaces

    Directory of Open Access Journals (Sweden)

    Crnomarković Nenad Đ.

    2016-01-01

    Full Text Available The influence of the number of gray gases in the weighted sum in the gray gases model on the calculation of the radiative heat transfer is discussed in the paper. A computer code which solved the set of equations of the mathematical model describing the reactive two-phase turbulent flow with radiative heat exchange and with thermal equilibrium between phases inside the pulverized coal-fired furnace was used. Gas-phase radiative properties were determined by the simple gray gas model and two combinations of the weighted sum of the gray gases models: one gray gas plus a clear gas and two gray gases plus a clear gas. Investigation was carried out for two values of the total extinction coefficient of the dispersed phase, for the clean furnace walls and furnace walls covered by an ash layer deposit, and for three levels of the approximation accuracy of the weighting coefficients. The influence of the number of gray gases was analyzed through the relative differences of the wall fluxes, wall temperatures, medium temperatures, and heat transfer rate through all furnace walls. The investigation showed that there were conditions of the numerical investigations for which the relative differences of the variables describing the radiative heat exchange decrease with the increase in the number of gray gases. The results of this investigation show that if the weighted sum of the gray gases model is used, the complexity of the computer code and calculation time can be reduced by optimizing the number of gray gases. [Projekat Ministarstva nauke Republike Srbije, br. TR-33018: Increase in energy and ecology efficiency of processes in pulverized coal-fired furnace and optimization of utility steam boiler air preheater by using in-house developed software tools

  1. Unburned Carbon Loss in Fly Ash of CFB Boilers Burning Hard Coal

    Institute of Scientific and Technical Information of China (English)

    L(U) Junfu(吕俊复); WANG Qimin(王启民); LI Yong(黎永); YUE Guangxi(岳光溪); Yam Y.Lee; Baldur Eliasson; SHEN Jiezhong(沈解忠); YU Long(于龙)

    2003-01-01

    The unburned carbon loss in fly ash of circulating fluidized bed (CFB) boilers, most of which are burning active fuels such as lignite or peat, is normally very low. However, most CFB boilers in China usually burn hard coals such as anthracite and bituminous coal and coal wastes, so the carbon content in the fly ash from these boilers is higher than expected. This paper investigates the source of unburned carbon in the fly ash of CFB boilers burning hard coal through a series of field tests and laboratory investigations. The char behavior during combustion, including fragmentation and deactivation, which is related to the parent coal, has an important impact on the carbon burnout in CFB boilers. The research shows that char deactivation occurs during char burnout in fluidized bed combustion, especially for large particles of low rank coal. The uneven mixing of solids and air in the core region of the furnace also causes poor burnout of carbon in CFB fly ash. An index describing the volatile content (as dry ash free basis) over the heating value is proposed to present the coal rank. The coal combustion efficiency is shown to be strongly connected with this coal index. Several changes in the CFB boiler design are suggested to reduce the unburned carbon loss in the fly ash.

  2. Engineering development of advanced coal-fired low-emissions boiler system. Phase II subsystem test design and plan - an addendum to the Phase II RD & T Plan

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1995-05-01

    Shortly after the year 2000 it is expected that new generating plants will be needed to meet the growing demand for electricity and to replace the aging plants that are nearing the end of their useful service life. The plants of the future will need to be extremely clean, highly efficient and economical. Continuing concerns over acid rain, air toxics, global climate changes, ozone depletion and solid waste disposal are expected to further then regulations. In the late 1980`s it was commonly believed that coal-fired power plants of the future would incorporate either some form of Integrated Gasification Combined Cycle (IGCC) or first generation Pressurized Fluidized Bed Combustion (PFBS) technologies. However, recent advances In emission control techniques at reduced costs and auxiliary power requirements coupled with significant improvements In steam turbine and cycle design have clearly indicated that pulverized coal technology can continue to be competitive In both cost and performance. In recognition of the competitive potential for advanced pulverized coal-fired systems with other emerging advanced coal-fired technologies, DOE`s Pittsburgh Energy Technology Center (PETC) began a research and development initiative In late 1990 named, Combustion 2000, with the intention of preserving and expanding coal as a principal fuel In the Generation of electrical power. The project was designed for two stages of commercialization, the nearer-term Low Emission Boiler System (LEBS) program, and for the future, the High Performance Power System (HIPPS) program. B&W is participating In the LEBS program.

  3. Boiler Briquette Coal versus Raw Coal: Part I-Stack Gas Emissions.

    Science.gov (United States)

    Ge, Su; Bai, Zhipeng; Liu, Weili; Zhu, Tan; Wang, Tongjian; Qing, Sheng; Zhang, Junfeng

    2001-04-01

    Stack gas emissions were characterized for a steam-generating boiler commonly used in China. The boiler was tested when fired with a newly formulated boiler briquette coal (BB-coal) and when fired with conventional raw coal (R-coal). The stack gas emissions were analyzed to determine emission rates and emission factors and to develop chemical source profiles. A dilution source sampling system was used to collect PM on both Teflon membrane filters and quartz fiber filters. The Teflon filters were analyzed gravimetrically for PM10 and PM2.5 mass concentrations and by X-ray fluorescence (XRF) for trace elements. The quartz fiber filters were analyzed for organic carbon (OC) and elemental carbon (EC) using a thermal/optical reflectance technique. Sulfur dioxide was measured using the standard wet chemistry method. Carbon monoxide was measured using an Orsat combustion analyzer. The emission rates of the R-coal combustion (in kg/hr), determined using the measured stack gas concentrations and the stack gas emission rates, were 0.74 for PM10, 0.38 for PM25, 20.7 for SO2, and 6.8 for CO, while those of the BB-coal combustion were 0.95 for PM10, 0.30 for PM2 5, 7.5 for SO2, and 5.3 for CO. The fuel-mass-based emission factors (in g/kg) of the R-coal, determined using the emission rates and the fuel burn rates, were 1.68 for PM10, 0.87 for PM25, 46.7 for SO2, and 15 for CO, while those of the BB-coal were 2.51 for PM10, 0.79 for PM2.5, 19.9 for SO2, and 14 for CO. The task-based emission factors (in g/ton steam generated) of the R-coal, determined using the fuel-mass-based emission factors and the coal/ steam conversion factors, were 0.23 for PM10, 0.12 for PM2.5, 6.4 for SO2, and 2.0 for CO, while those of the BB-coal were 0.30 for PM10, 0.094 for PM2.5, 2.4 for SO2, and 1.7 for CO. PM10 and PM2.5 elemental compositions are also presented for both types of coal tested in the study.

  4. Boiler briquette coal versus raw coal: Part I--Stack gas emissions.

    Science.gov (United States)

    Ge, S; Bai, Z; Liu, W; Zhu, T; Wang, T; Qing, S; Zhang, J

    2001-04-01

    Stack gas emissions were characterized for a steam-generating boiler commonly used in China. The boiler was tested when fired with a newly formulated boiler briquette coal (BB-coal) and when fired with conventional raw coal (R-coal). The stack gas emissions were analyzed to determine emission rates and emission factors and to develop chemical source profiles. A dilution source sampling system was used to collect PM on both Teflon membrane filters and quartz fiber filters. The Teflon filters were analyzed gravimetrically for PM10 and PM2.5 mass concentrations and by X-ray fluorescence (XRF) for trace elements. The quartz fiber filters were analyzed for organic carbon (OC) and elemental carbon (EC) using a thermal/optical reflectance technique. Sulfur dioxide was measured using the standard wet chemistry method. Carbon monoxide was measured using an Orsat combustion analyzer. The emission rates of the R-coal combustion (in kg/hr), determined using the measured stack gas concentrations and the stack gas emission rates, were 0.74 for PM10, 0.38 for PM2.5, 20.7 for SO2, and 6.8 for CO, while those of the BB-coal combustion were 0.95 for PM10, 0.30 for PM2.5, 7.5 for SO2, and 5.3 for CO. The fuel-mass-based emission factors (in g/kg) of the R-coal, determined using the emission rates and the fuel burn rates, were 1.68 for PM10, 0.87 for PM2.5, 46.7 for SO2, and 15 for CO, while those of the BB-coal were 2.51 for PM10, 0.79 for PM2.5, 19.9 for SO2, and 14 for CO. The task-based emission factors (in g/ton steam generated) of the R-coal, determined using the fuel-mass-based emission factors and the coal/steam conversion factors, were 0.23 for PM10, 0.12 for PM2.5, 6.4 for SO2, and 2.0 for CO, while those of the BB-coal were 0.30 for PM10, 0.094 for PM2.5, 2.4 for SO2, and 1.7 for CO. PM10 and PM2.5 elemental compositions are also presented for both types of coal tested in the study.

  5. Inquiry into Safety Problems in Production of Shell Pulverized Coal Gasifier%Shell粉煤气化生产中安全问题的探讨

    Institute of Scientific and Technical Information of China (English)

    于英慧

    2011-01-01

    详细介绍了Shell粉煤气化工艺生产过程中常见的安全异常情况.探讨并提出了Shell粉煤气化工艺不同工段的安全措施.%Details are given of common abnormal conditions in safety during Shell pulverized coal gasification. An inquiry is made and safety measures are proposed for the various sections of the Shell pulverized coal gasification process.

  6. Effective identification of the three particle modes generated during pulverized coal combustion

    Institute of Scientific and Technical Information of China (English)

    YU DunXi; XU MingHou; YAO Hong; LIU XiaoWei; ZHOU Ke

    2008-01-01

    Based on the mass fraction size distribution of aluminum (AI), an improved method for effectively identifying the modes of particulate matter from pulverized coal combustion is proposed in this study. It is found that the particle size distributions of coal-derived particulate matter actually have three modes, rather than just mere two. The ultrafine mode is mainly generated through the vaporization and condensation processes. The coarse mode is primarily formed by the coalescence of molten minerals, while the newly-found central mode is attributed to the heterogeneous condensation or adsorption of vaporized species on fine residual ash particles. The detailed investigation of the mass fraction size distribution of sulfur (S) further demonstrates the rationality and effectiveness of the mass fraction size distribution of the AI in identifying three particle modes. The results show that not only can the number of particle modes be identified in the mass fraction size distributions of the AI but also can their size boundaries be more accurately defined. This method provides new insights in elucidating particle formation mechanisms and their physico-chemical characteristics.

  7. Boiler materials for ultra supercritical coal power plants

    Energy Technology Data Exchange (ETDEWEB)

    Purgert, Robert [Energy Industries of Ohio, Independence, OH (United States); Shingledecker, John [Electric Power Research Inst., Palo Alto, CA (United States); Pschirer, James [Alstom Power Inc., Windsor, CT (Untied States); Ganta, Reddy [Alstom Power Inc., Windsor, CT (Untied States); Weitzel, Paul [The Babcock & Wilcox Company, Baberton, OH (United States); Sarver, Jeff [The Babcock & Wilcox Company, Baberton, OH (United States); Vitalis, Brian [Riley Power Inc., Worchester, WA (United States); Gagliano, Michael [Foster Wheeler North America Corp., Hampton, NJ (United States); Stanko, Greg [Foster Wheeler North America Corp., Hampton, NJ (United States); Tortorelli, Peter [Oak Ridge National Lab. (ORNL), Oak Ridge, TN (United States)

    2015-12-29

    The U.S. Department of Energy (DOE) and the Ohio Coal Development Office (OCDO) have undertaken a project aimed at identifying, evaluating, and qualifying the materials needed for the construction of the critical components of coal-fired boilers capable of operating at much higher efficiencies than current generation of supercritical plants. This increased efficiency is expected to be achieved principally through the use of advanced ultrasupercritical (A-USC) steam conditions up to 760°C (1400°F) and 35 MPa (5000 psi). A limiting factor to achieving these higher temperatures and pressures for future A-USC plants are the materials of construction. The goal of this project is to assess/develop materials technology to build and operate an A-USC boiler capable of delivering steam with conditions up to 760°C (1400°F)/35 MPa (5000 psi). The project has successfully met this goal through a focused long-term public-private consortium partnership. The project was based on an R&D plan developed by the Electric Power Research Institute (EPRI) and an industry consortium that supplemented the recommendations of several DOE workshops on the subject of advanced materials. In view of the variety of skills and expertise required for the successful completion of the proposed work, a consortium led by the Energy Industries of Ohio (EIO) with cost-sharing participation of all the major domestic boiler manufacturers, ALSTOM Power (Alstom), Babcock and Wilcox Power Generation Group, Inc. (B&W), Foster Wheeler (FW), and Riley Power, Inc. (Riley), technical management by EPRI and research conducted by Oak Ridge National Laboratory (ORNL) has been developed. The project has clearly identified and tested materials that can withstand 760°C (1400°F) steam conditions and can also make a 700°C (1300°F) plant more economically attractive. In this project, the maximum temperature capabilities of these and other available high-temperature alloys have been assessed to provide a basis for

  8. Utilization of coal-water fuels in fire-tube boilers

    Energy Technology Data Exchange (ETDEWEB)

    Morrison, D.K.; Melick, T.A.; Sommer, T.M. [Energy and Environmental Research Corp., Orrville, OH (United States)

    1993-12-31

    The Energy and Environmental Research Corporation (EER), in cooperation with the University of Alabama and Jim Walter Resources, was awarded a DOE contract to retrofit an existing fire-tube boiler with a coal-water slurry (CWS) firing system. Recognizing that combustion efficiency is the principle concern when firing slurry in fire-tube boilers, EER has focused the program on innovative approaches for improving carbon burnout without major modifications to the boiler. The boiler was successfully operated on coal-water slurry for 800 hours. A boiler derate of 20 percent was necessary for successful operation with slurry accounting 62 percent of the total heat input with the balance provided by natural gas. Under these boiler conditions, the carbon conversion was 90 percent. Further data evaluation, a market analysis, and final report preparation remain to be completed.

  9. NOx Control Options and Integration for US Coal Fired Boilers

    Energy Technology Data Exchange (ETDEWEB)

    Mike Bockelie; Kevin Davis; Temi Linjewile; Connie Senior; Eric Eddings; Kevin Whitty; Larry Baxter; Calvin Bartholomew; William Hecker; Stan Harding; Robert Hurt

    2003-12-31

    This is the fourteenth Quarterly Technical Report for DOE Cooperative Agreement No: DEFC26-00NT40753. The goal of the project is to develop cost effective analysis tools and techniques for demonstrating and evaluating low NOx control strategies and their possible impact on boiler performance for boilers firing US coals. The Electric Power Research Institute (EPRI) is providing co-funding for this program. Using the initial CFD baseline modeling of the Gavin Station and the plant corrosion maps, six boiler locations for the corrosion probes were identified and access ports have been installed. Preliminary corrosion data obtained appear consistent and believable. In situ, spectroscopic experiments at BYU reported in part last quarter were completed. New reactor tubes have been made for BYU's CCR that allow for testing smaller amounts of catalyst and thus increasing space velocity; monolith catalysts have been cut and a small reactor that can accommodate these pieces for testing is in its final stages of construction. A poisoning study on Ca-poisoned catalysts was begun this quarter. A possible site for a biomass co-firing test of the slipstream reactor was visited this quarter. The slipstream reactor at Rockport required repair and refurbishment, and will be re-started in the next quarter. This report describes the final results of an experimental project at Brown University on the fundamentals of ammonia / fly ash interactions with relevance to the operation of advanced NOx control technologies such as selective catalytic reduction. The Brown task focused on the measurement of ammonia adsorption isotherms on commercial fly ash samples subjected to a variety of treatments and on the chemistry of dry and semi-dry ammonia removal processes.

  10. Effect of CO2 gasification reaction on oxycombustion of pulverized coal char.

    Energy Technology Data Exchange (ETDEWEB)

    Molina, Alejandro (Universidad Nacional de Colombia, Medellin, Colombia); Hecht, Ethan S.; Shaddix, Christopher R.; Haynes, Brian S. (University of Sydney, New South Wales, Australia)

    2010-07-01

    For oxy-combustion with flue gas recirculation, as is commonly employed, it is recognized that elevated CO{sub 2} levels affect radiant transport, the heat capacity of the gas, and other gas transport properties. A topic of widespread speculation has concerned the effect of the CO{sub 2} gasification reaction with coal char on the char burning rate. To give clarity to the likely impact of this reaction on the oxy-fuel combustion of pulverized coal char, the Surface Kinetics in Porous Particles (SKIPPY) code was employed for a range of potential CO{sub 2} reaction rates for a high-volatile bituminous coal char particle (130 {micro}m diameter) reacting in several O{sub 2} concentration environments. The effects of boundary layer chemistry are also examined in this analysis. Under oxygen-enriched conditions, boundary layer reactions (converting CO to CO{sub 2}, with concomitant heat release) are shown to increase the char particle temperature and burning rate, while decreasing the O{sub 2} concentration at the particle surface. The CO{sub 2} gasification reaction acts to reduce the char particle temperature (because of the reaction endothermicity) and thereby reduces the rate of char oxidation. Interestingly, the presence of the CO{sub 2} gasification reaction increases the char conversion rate for combustion at low O{sub 2} concentrations, but decreases char conversion for combustion at high O{sub 2} concentrations. These calculations give new insight into the complexity of the effects from the CO{sub 2} gasification reaction and should help improve the understanding of experimentally measured oxy-fuel char combustion and burnout trends in the literature.

  11. Nitric oxide formation mechanisms, and their computation in pulverized coal combustion

    Energy Technology Data Exchange (ETDEWEB)

    Flour, I.; Dal Secco, S.

    1995-10-01

    This report consists of a review of several articles on nitric oxide emissions from coal-fired furnace. Three mechanisms have been identified, depending on the initial nitrogen sources and the composition of specific flame regions: - thermal-NO, formed from molecular nitrogen in the combustion products region at high temperature, - prompt-NO, formed from molecular nitrogen in the oxidation zone, - fuel-NO, formed from the fuel-bound nitrogen, partly during the coal pyrolysis (homogeneous reactions) and partly through reactions on the surface of the particle. In the combustion of pulverized coal, the fuel-NO mechanism accounts for the main source of nitric oxide formed. Detailed schemes of those reactions - when available - are too much complex to be used in tri-dimensional computation of pollutant emissions in furnaces of practical interest. According to the literature, reduced schemes seem to have been applied most frequently. The reaction schemes for the fuel-NO and the prompt-NO are based on the results of De Soete. For the homogeneous reactions, the intermediate species formed is assumed to be mainly HCN, leading to both formation and reduction reactions for NO, depending on the flame region. The formation of nitric oxide from the char-bound nitrogen, through heterogeneous reactions on the surface on the particle, is modelled by assuming the char-bound nitrogen to be released as HCN, with a rate proportional to char combustion. The released char nitrogen then reacts through the same path as the HCN released during pyrolysis. In the thermal-NO mechanism, nitric oxide is formed from molecular nitrogen, through the extended Zeldovich mechanism. This scheme contains radical species (O, N), which concentrations are assumed to be determined from the stationary condition or the equilibrium assumption. However, in spite of the use of reduced schemes for NO formation, the modelling of the important effect of the turbulent fluctuations has to be taken into account.

  12. NOx Control Options and Integration for US Coal Fired Boilers

    Energy Technology Data Exchange (ETDEWEB)

    Mike Bockelie; Kevin Davis; Temi Linjewile; Connie Senior; Eric Eddings; Kevin Whitty; Larry Baxter; Calvin Bartholomew; William Hecker; Stan Harding

    2003-06-30

    This is the twelfth Quarterly Technical Report for DOE Cooperative Agreement No: DE-FC26-00NT40753. The goal of the project is to develop cost effective analysis tools and techniques for demonstrating and evaluating low NOx control strategies and their possible impact on boiler performance for boilers firing US coals. The Electric Power Research Institute (EPRI) is providing co-funding for this program. This program contains multiple tasks and good progress is being made on all fronts. During this quarter, a new effort was begun on the development of a corrosion management system for minimizing the impacts of low NOx combustion systems on waterwalls; a kickoff meeting was held at the host site, AEP's Gavin Plant, and work commenced on fabrication of the probes. FTIR experiments for SCR catalyst sulfation were finished at BYU and indicated no vanadium/vanadyl sulfate formation at reactor conditions. Improvements on the mass-spectrometer system at BYU have been made and work on the steady state reactor system shakedown neared completion. The slipstream reactor continued to operate at AEP's Rockport plant; at the end of the quarter, the catalysts had been exposed to flue gas for about 1000 hours. Some operational problems were addressed that enable the reactor to run without excessive downtime by the end of the quarter.

  13. NOx Control Options and Integration for US Coal Fired Boilers

    Energy Technology Data Exchange (ETDEWEB)

    Mike Bockelie; Kevin Davis; Martin Denison; Connie Senior; Hong-Shig Shim; Darren Shino; Dave Swenson; Larry Baxter; Calvin Bartholomew; William Hecker

    2005-06-30

    This is the twentieth Quarterly Technical Report for DOE Cooperative Agreement No: DEFC26-00NT40753. The goal of the project is to develop cost-effective analysis tools and techniques for demonstrating and evaluating low-NO{sub x} control strategies and their possible impact on boiler performance for boilers firing US coals. The Electric Power Research Institute (EPRI) is providing co-funding for this program. At the beginning of this quarter, the corrosion probes were removed from Gavin Station. Data analysis and preparation of the final report continued this quarter. This quarterly report includes further results from the BYU catalyst characterization lab and the in-situ FTIR lab, and includes the first results from tests run on samples cut from the commercial plate catalysts. The SCR slipstream reactor at Plant Gadsden was removed from the plant, where the total exposure time on flue gas was 350 hours. A computational framework for SCR deactivation was added to the SCR model.

  14. NOx Control Options and Integration for US Coal Fired Boilers

    Energy Technology Data Exchange (ETDEWEB)

    Mike Bockelie; Kevin Davis; Temi Linjewile; Connie Senior; Eric Eddings; Kevin Whitty; Larry Baxter; Calvin Bartholomew; William Hecker; Stan Harding

    2004-03-31

    This is the fifteenth Quarterly Technical Report for DOE Cooperative Agreement No: DE-FC26-00NT40753. The goal of the project is to develop cost effective analysis tools and techniques for demonstrating and evaluating low NOx control strategies and their possible impact on boiler performance for boilers firing US coals. The Electric Power Research Institute (EPRI) is providing co-funding for this program. At AEP's Gavin Plant, data from the corrosion probes showed that corrosion rate increased as boiler load was increased. During an outage at the plant, the drop in boiler load, sensor temperature and corrosion rate could all be seen clearly. Restarting the boiler saw a resumption of corrosion activity. This behavior is consistent with previous observations made at a 600MWe utility boiler. More data are currently being examined for magnitudes of corrosion rates and changes in boiler operating conditions. Considerable progress was made this quarter in BYU's laboratory study of catalyst deactivation. Surface sulfation appears to partially suppress NO adsorption when the catalyst is not exposed to NH3; NH3 displaces surface-adsorbed NO on SCR catalysts and surface sulfation increases the amount of adsorbed NH3, as confirmed by both spectroscopy and TPD experiments. However, there is no indication of changes in catalyst activity despite changes in the amount of adsorbed NH3. A monolith test reactor (MTR), completed this quarter, provided the first comparative data for one of the fresh and field-exposed monolith SCR catalysts yet developed in this project. Measurements of activity on one of the field-exposed commercial monolith catalysts do not show significant changes in catalyst activity (within experimental error) as compared to the fresh catalyst. The exposed surface of the sample contains large amounts of Ca and Na, neither of which is present in the fresh sample, even after removal of visibly obvious fouling deposits. However, these fouling compounds do

  15. FY 2000 Report on the results of international cooperative research scheme (power generation - No.3). Developmental research on high-performance plasma-assisted fine coal powder combustion mechanism for coal-fired power generation boilers to realize oilless ignition; 2000 nendo kokusai kyodo kenkyu teian kobo jigyo seika hokokusho (hatsuden No.3). Oilless chakka wo jitsugensuru sekitan karyoku hatsuden bifuntan nenshoroyo koseino plasma jonen kiko no kaihatsu kenkyu

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    2001-03-01

    Described herein are the results of the developmental research on the high-performance plasma-assisted fine coal powder combustion mechanism for coal-fired power generation boilers, a theme adopted by the international cooperative research scheme. The program for design/manufacture of the plasma torch manufactures laminar type torches for 100kW high power class and 10kW middle class. The high-performance plasma-assisted combustion mechanism is designed and manufactured using the torch. It has a structure which supplies secondary air and secondary coal flow to the primary coal flow. It is tested for starting up a commercial boiler firing finely pulverized coal, to confirm its functions. The tests for optimizing the oilless ignition and operation are conducted in Tashtagonal Iron Plant and Berdsk Chemical Plant. It is found that the cold start can be realized in the boiler, when the muffle burners are preheated for 30 to 40 minutes before the finely pulverized coal is supplied and the steady-state coal combustion is attained 3 to 5 minutes after the coal is supplied. The program for the combustion basics for the plasma-assisted mechanism collects the data related to its dependence on coal type. (NEDO)

  16. Studying flame combustion of coal-water slurries in the furnaces of power-generating boilers

    Science.gov (United States)

    Osintsev, K. V.

    2012-06-01

    Matters concerned with organizing combustion of different types of coal-water slurries in coalfired boilers at thermal power stations are considered. Recommendations for improving the economic and environmental indicators and for achieving more reliable operation of furnace devices and boiler as a whole are given.

  17. APPLICATION OF REBURNING TO COAL-FIRED INDUSTRIAL BOILERS IN TAIWAN

    Science.gov (United States)

    The paper gives an overview of the characteristics of coal-fired industrial boilers in Taiwan and projections of the cost and performance data for retrofitting several boilers with reburning. The impacts of reburning fuel type on the reburning system design and cost effectivenes...

  18. COST OF SELECTIVE CATALYTIC REDUCTION (SCR) APPLICATION FOR NOX CONTROL ON COAL-FIRED BOILERS

    Science.gov (United States)

    The report provides a methodology for estimating budgetary costs associated with retrofit applications of selective catalytic reduction (SCR) technology on coal-fired boilers. SCR is a postcombustion nitrogen oxides (NOx) control technology capable of providing NOx reductions >90...

  19. Sulfur release from Ohio coals and sorbent kinetics in pulverized coal flames. Final report

    Energy Technology Data Exchange (ETDEWEB)

    Essenhigh, R. [Ohio State Univ., Columbus, OH (United States). Robinson Lab.

    1992-08-01

    In this report we describe the results of investigations into the structure of combustion and sulfur release profiles from coal burning in One-Dimensional P.C. flames using a furnace of unique design for the measurements. Selected measurements were also-carried out in a special high-intensity furnace also of unique design. The formal project work started in late Fall 1989, with unfunded preliminary work in the months prior to that. The process of limestone injection into the flame to control sulfur oxides emissions is a long-standing concept that has been given particular formulation in the LIMB process, and studies of such systems provide bases for commercial system economics. Problems with LIMB and related systems indicated need for better understanding of, jointly, the sulfur release from the coal and the sorbent behavior by the limestone. The investigations as reported in Vol. 1 of this Report used 14 different coals under a range of different initial and operating conditions, and the resulting measurements have provided a database of major proportions, as tabulated in the attached Volumes 2, 3, 4, 5, 6, and 7 of this report. This database consists of sets of measurements totalling about 45,000 entries for all independent and dependent parameters involved. The independent parameters included: coal type (analysis), firing rate, stoichiometry (fuel/air ratio), and sorbent content of the

  20. COMPARISON OF PARTICLE SIZE DISTRIBUTIONS AND ELEMENTAL PARTITIONING FROM THE COMBUSTION OF PULVERIZED COAL AND RESIDUAL FUEL OIL

    Science.gov (United States)

    The paper gives results of experimental efforts in which three coals and a residual fuel oil were combusted in three different systems simulating process and utility boilers. Particloe size distributions (PSDs) were determined using atmospheric and low-pressure impaction, electr...

  1. Investigation of swirling flow mixing for application in an MHD pulverized coal combustor using isothermal modeling

    Energy Technology Data Exchange (ETDEWEB)

    Power, W. H.

    1980-05-01

    The purpose of this study was to investigate combustor reactant mixing with swirling oxidizer flow. The combustor configuration that was considered was designed to simulate a 4 lbm/sec mas flow pulverized coal combustor being tested in The University of Tennessee Space Institute MHD Facility. A one-fourth dimensionally scaled combustor model was developed for isothermal flow testing. A comparison was made of cold flow tests using 3 swirler designs with a base case oxidizer injector design of perforated plated which demonstrated acceptable performance in the 4 lbm/sec MHD combustor. The three swirlers that were evaluated were designed to allow a wide range of swirl intensity to be investigated. The design criterion of the swirler was the swirl number which has been related to swirler geometry. The results of the study showed that the swirlers that were tested fell short of the mixing characteristics displayed with the perforated plate base case oxidizer injector. Test data obtained with the cold flow model established that the actual swirl numbers of two of the swirlers were much lower than the design swirl numbers. Recirculation zones were defined for all configurations that were tested, and a comparison of velocity profiles was made for the configurations.

  2. 小型常压煤粉仓惰性气体保护系统设计及应用%Design and Application of Inert Gas Protection System to Small-Scale Atmospheric Pressure Pulverized Coal Bunker

    Institute of Scientific and Technical Information of China (English)

    徐尧; 王乃继; 肖翠微

    2012-01-01

    According to the fuel safety storage requirements of the pulverized coal-fired industrial boiler, in order to solve the coal spon- taneous combustion problems caused by CO content and the temperature increased in the coal bunker, with the related national standards and overseas design handbook, the design calculation method and system control plan of the inert gas protection system was provided for the small-scale atmospheric pressure pulverized coal bunker. According to the two coal bunkers with volume of 40 m^3 , an inert gas pro- tection system of the small-scale atmospheric pressure pulverized coal bunker was designed. When the CO content in the pulverized coal bunker reached at 1 200×10^-6 or the temperature at the any location of the bunker was over 70 ℃, the inert gas protection system would have a protection to the coal bunker with the automatic start, manual start or mechanical emergency start. The project cases were applied to verify the inert gas protection system. The result showed that when the storage value of the protective gas CO2 would be 355 kg, the low pressure CO2 inerting system applied to the protection of the pulverized coal bunker could remarkably reduce the risks of the pulverized coal spontaneous combustion.%为解决煤粉仓CO浓度或温度增高导致的自燃问题,根据煤粉工业锅炉系统燃料安全储存需求,参照相关国家标准和国外设计手册,提出了小型常压煤粉仓惰性气体保护系统设计计算方法和系统控制方案。针对2台容积40m^3的煤粉仓设计了小型常压煤粉仓惰性气体保护系统,当检测到煤粉仓内CO体积分数达1200×10^-6或任意一处温度高于70℃时,系统可通过自动启动、手动启动、机械应急启动3种方式对煤粉仓保护,结合工程实例对该系统予以验证。结果表明:采用低压CO2惰化系统对煤粉仓实施保护,当保护气体CO2的储存量为355kg,可明显降低煤粉自燃的风险。

  3. An evaluation of deeply-cleaned coals as industrial boiler fuels

    Energy Technology Data Exchange (ETDEWEB)

    Miller, B.G.; Wincek, R.T.; Scaroni, A.W.

    1999-07-01

    AMAX Research and Development Center (AMAX) recently conducted a program for the US Department of Energy (DOE) in which processes for preparing ultra-clean coal were developed (Jha et al., 1997). The coal cleaning methods targeted were advanced column flotation and selective agglomeration. The goal was to develop a coal-based fuel, preferably a coal-water slurry fuel (CWSF), that would be a viable alternative to fuel oil or natural gas in industrial and utility boilers, and would also be appropriate for advanced combustion systems that are under development. Additional objectives were to develop near-term applications of the advanced coal cleaning technologies in new or existing coal preparation plants in order to efficiently process minus 28 mesh fines and convert them into marketable products, and to determine the extent of removal of toxic trace elements from coal by the advanced cleaning technologies. AMAX cleaned three coals in an integrated advanced column flotation and selective agglomeration process development unit. The coals were from the Taggart (Virginia), Indiana VII (Indiana) and Hiawatha (Utah) seams. As a complement to the AMAX program, Penn State is evaluating the deeply-cleaned coals as industrial boiler fuels. Specifically, the handling characteristics, combustion performance, and trace element emissions of the coals are being determined. The coals are being tested in demonstration (20 million Btu/h) and research (2 million Btu/h) boilers as part of a Penn State/DOE project characterizing trace element emissions from coal-fired industrial boilers. This paper will discuss the atomization characteristics and combustion performance (in the demonstration boiler) in a 1 ton/h filter cake re-entrainment circuit. In addition, the combustion performance of the ultra-clean CWSFs is compared to that of other CWSFs prepared in Penn State's 1 ton/h single and double-stage grinding circuit.

  4. Experimental investigation on NO{sub x} emission and carbon burnout from a radially biased pulverized coal whirl burner

    Energy Technology Data Exchange (ETDEWEB)

    Xue, Shan; Hui, Shi' en; Zhou, Qulan; Xu, Tongmo; Hu, Hongli [State Key Laboratory of Multiphase Flow in Power Engineering, School of Energy and Power Engineering, Xi' an Jiaotong University, Xi' an 710049 (China); Liu, Taisheng [Dongfang Boiler Group Co., Ltd., Zigong, Sichuan 643001 (China)

    2009-09-15

    Experiments have been performed on 1 MW pulverized coal (pc) furnace in order to investigate the characteristics of coal combustion and NO{sub x} emission from a new type of radially biased dual register whirl burner. The burner is characterized by a primary air pipe with a continuously changing cross-section and an impact ring. The mixture of pulverized coal and air inside the primary pipe is split into two streams, which are the outer pc rich annular jet and the inner pc lean annular jet respectively. Three Chinese coals, which are high rank bituminous coal, low rank bituminous coal and meager coal respectively, are used in the experiments. We examine the influences of various parameters such as the relative position of the over-fire air (OFA) nozzle, over-fire air ratio (19.1%), primary air ratio, inner secondary air ratio, outer secondary air ratio, inner secondary air swirling intensity, and outer secondary air swirling intensity on NO{sub x} formation and unburned carbon in fly ash. With the primary air ratio increasing from 13.4% to 23.4%, the value of the NO{sub x} emission of the SH coal decreases by 26.7% at first, and then increases by 21.7%. In contrast, the value of the carbon in fly ash (C{sub FA}) increases by 40.1% at first, and then decreases by 58.3%. According to the experimental results, the influence of each individual parameter on NO{sub x} formation and unburned carbon in fly ash agrees well with the existing literature. In this study, the influences of various combinations of these parameters are also examined, thus providing some reference for the design of the radial biased whirl burner, the configuration of the furnace and the distribution of the air. (author)

  5. NOx CONTROL OPTIONS AND INTEGRATION FOR US COAL FIRED BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    Mike Bockelie; Marc Cremer; Kevin Davis; Connie Senior; Bob Hurt; Eric Suuberg; Eric Eddings; Larry Baxter

    2002-01-31

    This is the sixth Quarterly Technical Report for DOE Cooperative Agreement No: DE-FC26-00NT40753. The goal of the project is to develop cost effective analysis tools and techniques for demonstrating and evaluating low NOx control strategies and their possible impact on boiler performance for firing US coals. The Electric Power Research Institute (EPRI) is providing co-funding for this program. This program contains multiple tasks and good progress is being made on all fronts. Preliminary results from laboratory and field tests of a corrosion probe to predict waterwall wastage indicate good agreement between the electrochemical noise corrosion rates predicted by the probe and corrosion rates measured by a surface profilometer. Four commercial manufacturers agreed to provide catalyst samples to the program. BYU has prepared two V/Ti oxide catalysts (custom, powder form) containing commercially relevant concentrations of V oxide and one containing a W oxide promoter. Two pieces of experimental apparatus being built at BYU to carry out laboratory-scale investigations of SCR catalyst deactivation are nearly completed. A decision was made to carry out the testing at full-scale power plants using a slipstream of gas instead of at the University of Utah pilot-scale coal combustor as originally planned. Design of the multi-catalyst slipstream reactor was completed during this quarter. One utility has expressed interest in hosting a long-term test at one of their plants that co-fire wood with coal. Tests to study ammonia adsorption onto fly ash have clearly established that the only routes that can play a role in binding significant amounts of ammonia to the ash surface, under practical ammonia slip conditions, are those that must involve co-adsorbates.

  6. Coal Direct Chemical Looping Retrofit to Pulverized Coal Power Plants for In-Situ CO2 Capture

    Energy Technology Data Exchange (ETDEWEB)

    Zeng, Liang; Li, Fanxing; Kim, Ray; Bayham, Samuel; McGiveron, Omar; Tong, Andrew; Connell, Daniel; Luo, Siwei; Sridhar, Deepak; Wang, Fei; Sun, Zhenchao; Fan, Liang-Shih

    2013-09-30

    A novel Coal Direct Chemical Looping (CDCL) system is proposed to effectively capture CO2 from existing PC power plants. The work during the past three years has led to an oxygen carrier particle with satisfactory performance. Moreover, successful laboratory, bench scale, and integrated demonstrations have been performed. The proposed project further advanced the novel CDCL technology to sub-pilot scale (25 kWth). To be more specific, the following objectives attained in the proposed project are: 1. to further improve the oxygen carrying capacity as well as the sulfur/ash tolerance of the current (working) particle; 2. to demonstrate continuous CDCL operations in an integrated mode with > 99% coal (bituminous, subbituminous, and lignite) conversion as well as the production of high temperature exhaust gas stream that is suitable for steam generation in existing PC boilers; 3. to identify, via demonstrations, the fate of sulfur and NOx; 4. to conduct thorough techno-economic analysis that validates the technical and economical attractiveness of the CDCL system. The objectives outlined above were achieved through collaborative efforts among all the participants. CONSOL Energy Inc. performed the techno-economic analysis of the CDCL process. Shell/CRI was able to perform feasibility and economic studies on the large scale particle synthesis and provide composite particles for the sub-pilot scale testing. The experience of B&W (with boilers) and Air Products (with handling gases) assisted the retrofit system design as well as the demonstration unit operations. The experience gained from the sub-pilot scale demonstration of the Syngas Chemical Looping (SCL) process at OSU was able to ensure the successful handling of the solids. Phase 1 focused on studies to improve the current particle to better suit the CDCL operations. The optimum operating conditions for the reducer reactor such as the temperature, char gasification enhancer type, and flow rate were identified. The

  7. [Emission characteristics of PM10 from coal-fired industrial boiler].

    Science.gov (United States)

    Li, Chao; Li, Xing-Hua; Duan, Lei; Zhao, Meng; Duan, Jing-Chun; Hao, Ji-Ming

    2009-03-15

    Through ELPI (electrical low-pressure impactor) based dilution sampling system, the emission characteristics of PM10 and PM2.5 was studied experimentally at the inlet and outlet of dust catchers at eight different coal-fired industrial boilers. Results showed that a peak existed at around 0.12-0.20 microm of particle size for both number size distribution and mass size distribution of PM10 emitted from most of the boilers. Chemical composition analysis indicated that PM2.5 was largely composed of organic carbon, elementary carbon, and sulfate, with mass fraction of 3.7%-21.4%, 4.2%-24.6%, and 1.5%-55.2% respectively. Emission factors of PM10 and PM2.5 measured were 0.13-0.65 kg x t(-1) and 0.08-0.49 kg x t(-1) respectively for grate boiler using raw coal, and 0.24 kg x t(-1) and 0.22 kg x t(-1) for chain-grate boiler using briquette. In comparison, the PM2.5 emission factor of fluidized bed boiler is 1.14 kg x t(-1), much her than that of grate boiler. Due to high coal consumption and low efficiency of dust separator, coal-fired industrial boiler may become the most important source of PM10, and should be preferentially controlled in China.

  8. Multi-objective Optimization of Coal-fired Boiler Combustion Based on NSGA-II

    Directory of Open Access Journals (Sweden)

    Tingfang Yu

    2013-06-01

    Full Text Available NOx emission characteristics and overall heat loss model for a 300MW coal-fired boiler were established by Back Propagation (BP neural network, by which the the functional relationship between outputs (NOx emissions & overall heat loss of the boiler and inputs (operational parameters of the boiler of a coal-fired boiler can be predicted. A number of field test data from a full-scale operating 300MWe boiler were used to train and verify the BP model. The NOx emissions & heat loss predicted by the BP neural network model showed good agreement with the measured. Then, BP model and the non-dominated sorting genetic algorithm II (NSGA-II were combined to gain the optimal operating parameters which lead to lower NOx emissions and overall heat loss boiler. The optimization results showed that hybrid algorithm by combining BP neural network with NSGA-II can be a good tool to solve the problem of multi-objective optimization of a coal-fired combustion, which can reduce NOx emissions and overall heat loss effectively for the coal-fired boiler.

  9. MINIMIZATION OF NO EMISSIONS FROM MULTI-BURNER COAL-FIRED BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    E.G. Eddings; A. Molina; D.W. Pershing; A.F. Sarofim; T.H. Fletcher; H. Zhang; K.A. Davis; M. Denison; H. Shim

    2002-01-01

    The focus of this program is to provide insight into the formation and minimization of NO{sub x} in multi-burner arrays, such as those that would be found in a typical utility boiler. Most detailed studies are performed in single-burner test facilities, and may not capture significant burner-to-burner interactions that could influence NO{sub x} emissions. Thus, investigations of such interactions were made by performing a combination of single and multiple burner experiments in a pilot-scale coal-fired test facility at the University of Utah, and by the use of computational combustion simulations to evaluate full-scale utility boilers. In addition, fundamental studies on nitrogen release from coal were performed to develop greater understanding of the physical processes that control NO formation in pulverized coal flames--particularly under low NO{sub x} conditions. A CO/H{sub 2}/O{sub 2}/N{sub 2} flame was operated under fuel-rich conditions in a flat flame reactor to provide a high temperature, oxygen-free post-flame environment to study secondary reactions of coal volatiles. Effects of temperature, residence time and coal rank on nitrogen evolution and soot formation were examined. Elemental compositions of the char, tar and soot were determined by elemental analysis, gas species distributions were determined using FTIR, and the chemical structure of the tar and soot was analyzed by solid-state {sup 13}C NMR spectroscopy. A laminar flow drop tube furnace was used to study char nitrogen conversion to NO. The experimental evidence and simulation results indicated that some of the nitrogen present in the char is converted to nitric oxide after direct attack of oxygen on the particle, while another portion of the nitrogen, present in more labile functionalities, is released as HCN and further reacts in the bulk gas. The reaction of HCN with NO in the bulk gas has a strong influence on the overall conversion of char-nitrogen to nitric oxide; therefore, any model that

  10. NOx CONTROL OPTIONS AND INTEGRATION FOR US COAL FIRED BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    Mike Bockelie; Marc Cremer; Kevin Davis; Temi Linjewile; Connie Senior; Hong-Shig Shim; Bob Hurt; Eric Eddings; Larry Baxter

    2003-01-30

    This is the tenth Quarterly Technical Report for DOE Cooperative Agreement No: DE-FC26-00NT40753. The goal of the project is to develop cost effective analysis tools and techniques for demonstrating and evaluating low NO{sub x} control strategies and their possible impact on boiler performance for firing US coals. The Electric Power Research Institute (EPRI) is providing cofunding for this program. This program contains multiple tasks and good progress is being made on all fronts. During this quarter, progress was made on the computational simulation of a full-scale boiler with the purpose of understanding the potential impacts of burner operating conditions on soot and NO{sub x} generation. Sulfation tests on both the titania support and vanadia/titania catalysts were completed using BYU's in situ spectroscopy reactor this quarter. These experiments focus on the extent to which vanadia and titania sulfate in an SO{sub 2}-laden, moist environment. Construction of the CCS reactor system is essentially complete and the control hardware and software are largely in place. A large batch of vanadia/titania catalyst in powder form has been prepared for use in poisoning tests. During this quarter, minor modifications were made to the multi-catalyst slipstream reactor and to the control system. The slipstream reactor was installed at AEP's Rockport plant at the end of November 2002. In this report, we describe the reactor system, particularly the control system, which was created by REI specifically for the reactor, as well as the installation at Rockport.

  11. MINIMIZATION OF NO EMISSIONS FROM MULTI-BURNER COAL-FIRED BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    E.G.Eddings; A. Molina; D.W. Pershing; A.F. Sarofim; K.A. Davis; M.P. Heap; T.H. Fletcher; H. Zhang

    2001-06-01

    An initial testing campaign was carried out during the summer of 2000 to evaluate the impact of multiburner firing on NOx emissions. Extensive data had been collected during the Fall of 1999 and Spring of 2000 using a single pulverized-coal (PC) burner, and this data collection was funded by a separate Department of Energy program, the Combustion 2000 Low Emission Boiler System (LEBS) project under the direction of DB Riley. This single-burner data was thus available for comparison with NOx emissions obtained while firing three burners at the same overall load and operating conditions. A range of operating conditions were explored that were compatible with single-burner data, and thus the emission trends as a function of air staging, burner swirl and other parameters will be described below. In addition, a number of burner-to-burner operational variations were explored that provided interesing insight on their potential impact on NOx emissions. Some of these variations include: running one burner very fuel rich while running the others fuel lean; varying the swirl of a single burner while holding others constant; increasing the firing rate of a single burner while decreasing the others. In general, the results to date indicated that multiburner firing yielded higher NOx emissions than single burner firing at the same fuel rate and excess air. At very fuel rich burner stoichiometries (SR < 0.75), the difference between multiple and single burners became indistinguishable. This result is consistent with previous single-burner data that showed that at very rich stoichiometries the NOx emissions became independent of burner settings such as air distributions, velocities and burner swirl.

  12. Distribution and Fate of Mercury in Pulverized Bituminous Coal-Fired Power Plants in Coal Energy-Dominant Huainan City, China.

    Science.gov (United States)

    Chen, Bingyu; Liu, Guijian; Sun, Ruoyu

    2016-05-01

    A better understanding on the partitioning behavior of mercury (Hg) during coal combustion in large-scale coal-fired power plants is fundamental for drafting Hg-emission control regulations. Two large coal-fired utility boilers, equipped with electrostatic precipitators (ESPs) and a wet flue gas desulfurization (WFGD) system, respectively, in coal energy-dominant Huainan City, China, were selected to investigate the distribution and fate of Hg during coal combustion. In three sampling campaigns, we found that Hg in bottom ash was severely depleted with a relative enrichment (RE) index coal. We estimated that Hg emissions in all Huainan coal-fired power plants varied from 1.8 Mg in 2003 to 7.3 Mg in 2010.

  13. STUDY ON DOUBLE-CHANNEL CYCLONE-TYPE PULVERIZED COAL BURNER WITH INNER-POSITIONED FLAME-STABILIZING BODY AND ITS APPLICATION ON 410 t/h BOILER%加内置稳焰体的双通道旋流煤粉燃烧器研究及其在410 t/h锅炉上的应用

    Institute of Scientific and Technical Information of China (English)

    熊立红; 唐必光; 顾昌; 顾山; 高茂; 刘玲; 蔡建国

    2001-01-01

    The combustion-stabilizing mechanism of the title burner has been analyzed.The results of test,measurement and study of cold-state simulation have been given.Based on the results of study,the cyclone-type burner of boiler No 3 in Huozhou Power Plant,Shanxi province,has been retrofitted.The results of commercial experiments show,this kind of burner has better fire-stabilizing capability.%分析了加内置稳焰体的双通道旋流煤粉燃烧器的稳燃机理,给出了冷态模拟试验测量及研究结果,根据研究结果对山西霍州电厂3号炉的旋流燃烧器进行了改造。工业试验结果表明,该燃烧器具有较好的稳燃性能。

  14. Ash transformation in suspension fired boilers co-firing coal and straw

    DEFF Research Database (Denmark)

    Zheng, Yuanjing; Jensen, Peter Arendt; Jensen, Anker Degn

    In this literature report is provided a status for the present knowledge level on ash properties when co-firing coal and biomass. The fly ash formed in boilers using co-firing of coal and straw do have a large influence on ash deposit formation, boiler corrosion, fly ash utilization and operation...... of alkali getter experiments and a discussion of modeling of alkali reaction with kaolin. Presently there is still a need for a better understanding of especially the reaction of potassium with coal ash, thereby making better predictions of co-firing ash properties....

  15. Co-firing straw and coal in a 150-MWe utility boiler: in situ measurements

    DEFF Research Database (Denmark)

    Hansen, P. F.B.; Andersen, Karin Hedebo; Wieck-Hansen, K.;

    1998-01-01

    A 2-year demonstration program is carried out by the Danish utility I/S Midtkraft at a 150-MWe PF-boiler unit reconstructed for co-firing straw and coal. As a part of the demonstration program, a comprehensive in situ measurement campaign was conducted during the spring of 1996 in collaboration...... deposition propensities and high temperature corrosion during co-combustion of straw and coal in PF-boilers. Danish full scale results from co-firing straw and coal, the test facility and test program, and the potential theoretical support from the Technical University of Denmark are presented in this paper...

  16. Iron aluminide weld overlay coatings for boiler tube protection in coal-fired low NOx boilers

    Energy Technology Data Exchange (ETDEWEB)

    Banovic, S.W.; DuPont, J.N.; Marder, A.R. [Lehigh Univ., Bethlehem, PA (United States). Energy Research Center

    1997-12-01

    Iron aluminide weld overlay coatings are currently being considered for enhanced sulfidation resistance in coal-fired low NO{sub x} boilers. The use of these materials is currently limited due to hydrogen cracking susceptibility, which generally increases with an increase in aluminum concentration of the deposit. The overall objective of this program is to attain an optimum aluminum content with good weldability and improved sulfidation resistance with respect to conventional materials presently in use. Research has been initiated using Gas Tungsten Arc Welding (GTAW) in order to achieve this end. Under different sets of GTAW parameters (wire feed speed, current), both single and multiple pass overlays were produced. Characterization of all weldments was conducted using light optical microscopy, scanning electron microscopy, and electron probe microanalysis. Resultant deposits exhibited a wide range of aluminum contents (5--43 wt%). It was found that the GTAW overlays with aluminum contents above {approximately}10 wt% resulted in cracked coatings. Preliminary corrosion experiments of 5 to 10 wt% Al cast alloys in relatively simple H{sub 2}/H{sub 2}S gas mixtures exhibited corrosion rates lower than 304 stainless steel.

  17. Measurement of gas species, temperatures, coal burnout, and wall heat fluxes in a 200 MWe lignite-fired boiler with different overfire air damper openings

    Energy Technology Data Exchange (ETDEWEB)

    Jianping Jing; Zhengqi Li; Guangkui Liu; Zhichao Chen; Chunlong Liu [Harbin Institute of Technology, Harbin (China). School of Energy Science and Engineering

    2009-07-15

    Measurements were performed on a 200 MWe, wall-fired, lignite utility boiler. For different overfire air (OFA) damper openings, the gas temperature, gas species concentration, coal burnout, release rates of components (C, H, and N), furnace temperature, and heat flux and boiler efficiency were measured. Cold air experiments for a single burner were conducted in the laboratory. The double-swirl flow pulverized-coal burner has two ring recirculation zones starting in the secondary air region in the burner. As the secondary air flow increases, the axial velocity of air flow increases, the maxima of radial velocity, tangential velocity and turbulence intensity all increase, and the swirl intensity of air flow and the size of recirculation zones increase slightly. In the central region of the burner, as the OFA damper opening widens, the gas temperature and CO concentration increase, while the O{sub 2} concentration, NOx concentration, coal burnout, and release rates of components (C, H, and N) decrease, and coal particles ignite earlier. In the secondary air region of the burner, the O{sub 2} concentration, NOx concentration, coal burnout, and release rates of components (C, H, and N) decrease, and the gas temperature and CO concentration vary slightly. In the sidewall region, the gas temperature, O{sub 2} concentration, and NOx concentration decrease, while the CO concentration increases and the gas temperature varies slightly. The furnace temperature and heat flux in the main burning region decrease appreciably, but increase slightly in the burnout region. The NOx emission decreases from 1203.6 mg/m{sup 3} (6% O{sub 2}) for a damper opening of 0% to 511.7 mg/m{sup 3} (6% O{sub 2}) for a damper opening of 80% and the boiler efficiency decreases from 92.59 to 91.9%. 15 refs., 17 figs., 3 tabs.

  18. COMPUTATIONAL MODELING AND EXPERIMENTAL STUDIES ON NOx REDUCTION UNDER PULVERIZED COAL COMBUSTION CONDITIONS

    Energy Technology Data Exchange (ETDEWEB)

    Subha K. Kumpaty; Kannikeswaran Subramanian; Victor P. Nokku; Tyrus L. Hodges; Adel Hassouneh; Ansumana Darboe; Sravan K. Kumpati

    1998-06-01

    In this work, both computer simulation and experimental studies were conducted to investigate several strategies for NO{sub x} reduction under pulverized coal combustion conditions with an aim to meet the stringent environmental standards for NO{sub x} control. Both computer predictions and reburning experiments yielded favorable results in terms of NO{sub x} control by reburning with a combination of methane and acetylene as well as non-selective catalytic reduction of NO{sub x} with ammonia following reburning with methane. The greatest reduction was achieved at the reburning stoichiometric ratio of 0.9; the reduction was very significant, as clearly shown in Chapters III and V. Both the experimental and computational results favored mixing gases: methane and acetylene (90% and 10% respectively) and methane and ammonia (98% and 2%) in order to get optimum reduction levels which can not be achieved by individual gases at any amounts. Also, the above gaseous compositions as reburning fuels seemed to have a larger window of stoichiometric ratio (SR2 < 0.9) as opposed to just methane (SR2=0.9) so as to reduce and keep NO{sub x} at low ppm levels. From the various computational runs, it has been observed that although there are several pathways that contribute to NO{sub x} reduction, the key pathway is NO {r_arrow} HCN {r_arrow} NH{sub 3} {r_arrow} N{sub 2} + H{sub 2}. With the trends established in this work, it is possible to scale the experimental results to real time industrial applications using computational calculations.

  19. Pulverized coal injection on the blast furnaces at U.S. Steel Kosice, S.R.O.

    Energy Technology Data Exchange (ETDEWEB)

    Baran, P.; McCoy, M.; Szalona, T. [United States Steel Corp., Kosice (Slovakia)

    2008-07-01

    United States Steel Corporation at Kosice built a new modern PCI facility that meets environmental criteria and provides a replacement for financially demanding metallurgical coke with a less expensive pulverized coal. The pulverized coal injection (PCI) technology was applied to blast furnaces no. 2 and 3 in 1993 and has resulted in the following improvements: production has increased an average of 400 to 500 tons/day; pig iron production economics have improved not only because of replacing the metallurgical coke with PCI, but also due to a decrease in the total fuel rate for producing 1 ton of hot metal; blast furnace gas utilization increased with ETA CO values around 48 per cent; and the blast furnace operation is more stable by regular burden descend. The most distinguished change has been in the way raw materials are charged to the furnaces. This paper outlined the coal quality requirements for PCI and presented a basic technological description of PCI preparation. The operational experience of the 2 blast furnaces were presented for the period of 2000 to 2007. Recommendations for PCI rate increase were also presented. It was concluded that using PCI technology in blast furnace no. 1 may bring the greatest economic efficiency for United Steel Corporation at Kosice. 4 refs., 2 tabs., 8 figs.

  20. CFD investigation on the flow and combustion in a 300 MWe tangentially fired pulverized-coal furnace

    Science.gov (United States)

    Khaldi, Nawel; Chouari, Yoldoss; Mhiri, Hatem; Bournot, Philippe

    2016-09-01

    The characteristics of the flow, combustion and temperature in a 300 MWe tangentially fired pulverized-coal furnace are numerically studied using computational fluid dynamics. The mathematical model is based on a Eulerian description for the continuum phase and a Lagrangian description for coal particles. The combustion reaction scheme was modeled using eddy dissipation concept. The application of a proper turbulence model is mandatory to generate accurate predictions of flow and heat transfer during combustion. The current work presents a comparative study to identify the suitable turbulence model for tangentially fired furnace problem. Three turbulence models including the standard k-ɛ model, the RNG k-ɛ model and the Reynolds Stress model, RSM are examined. The predictions are compared with the published experimental data of Zheng et al. (Proc Combust Inst 29: 811-818, 2002). The RNG k-ɛ model proves to be the most suitable turbulence model, offering a satisfactory prediction of the velocity, temperature and species fields. The detailed results presented in this paper may enhance the understanding of complex flow patterns and combustion processes in tangentially fired pulverized-coal furnaces.

  1. 煤粉燃烧过程的数值模拟%Numerical simulation of pulverized-coal combustion

    Institute of Scientific and Technical Information of China (English)

    张宏博; 秦国彤; 纪任山; 王乃继

    2009-01-01

    The comparative study between CFD numerical results of pulverized coal combustion process and the experimental data is becoming an important measure for validating mathematical models and direct engineering practice. The CFD commercial software, FLUENT, was used to simulate the pulverized coal flow and combustion. Mixture-Fraction/PDF model was used to simulate turbulent combustion; P-1 radiation model was used for simulating radiation heat transfer; the Langrange/Euler's method was used for dealing with momentum, mass and energy exchange between the solid and the gas phase; the two-competing rates model for devolatilization and the kinitics/diffusion limited combustion model for simulating surface combustion of pulverized coal particles. The result of simulation is consistent with the data from actual combustion process. The simulation results show the rules of the volatile releasing and combustion processing of coke, which could provide important references to improve the combustion of the pulverized coal.%采用计算流体动力学软件对煤粉实际燃烧过程进行数值计算并结合其热态试验数据进行对比分析,已成为验证数学模型和指导工程实践的一种重要研究手段,应用商业软件FLUENT对煤粉燃烧及流场进行了数值模拟分析,采用混合分数/概率密度函数法模拟湍流燃烧,用P-1辐射模型开展辐射传热模拟,利用拉格朗日/欧拉法处理气固两相间的动量、质量和能量交换,对挥发份的析出采用双速率竞争模型,采用动力/扩散反应速率模型模拟煤粉颗粒的表面燃烧,并对模拟结果进行分析与对比,计算结果与实际燃烧过程有较好的一致性,数值模拟计算结果揭示了挥发分释放与焦炭燃烧的过程,为改善和优化煤粉的燃烧提供了重要的参考依据.

  2. Powder Leakage Cause Analysis and Control Measures of Double Cyclone Pulverized Coal Burner%双旋风煤粉燃烧器漏粉原因分析和控制措施

    Institute of Scientific and Technical Information of China (English)

    王勇; 蒋治其

    2015-01-01

    "W"type flame boiler burner is pulverized coal burner. Because of the large number and big size of the devices, the design layout is compact and there are many flange connections between devices. In order to ensure installation quality and operation safety of the burner, this article analyzes the causes and introduces the control measures of burner powder leakage from the aspect of installation.%“W”型火焰锅炉燃烧器为旋风煤粉燃烧器,因其设备多、设备尺寸较大,因而设计布置紧凑、设备间法兰连接较多。为保证燃烧器安装质量以及运行安全,本文从安装角度出发对燃烧器漏粉进行了原因分析和控制措施。

  3. Application of the decree 2910 for coal fired boilers; Application de l`arrete 2910 aux chaudieres a charbon

    Energy Technology Data Exchange (ETDEWEB)

    Hing, K. [CDF Energie, Charbonnages de France, 92 - Rueil-Malmaison (France)

    1997-12-31

    The impacts of the new French decree 2910 concerning the classification of all combustion equipment with regards to their energy sources, energy efficiency and pollution control, on 2 to 20 MW coal-fired boilers, are discussed, with emphasis on their pollutant emissions (SO{sub 2}, NO{sub x} and ashes). The compositions of several coals is presented and the various types of coal-fired boilers adapted to the new decree are presented: automatic boilers, dense fluidized bed boilers, vibrating and chain grids with fume tubes and water tubes

  4. An examination of heat rate improvements due to waste heat integration in an oxycombustion pulverized coal power plant

    Science.gov (United States)

    Charles, Joshua M.

    Oxyfuel, or oxycombustion, technology has been proposed as one carbon capture technology for coal-fired power plants. An oxycombustion plant would fire coal in an oxidizer consisting primarily of CO2, oxygen, and water vapor. Flue gas with high CO2 concentrations is produced and can be compressed for sequestration. Since this compression generates large amounts of heat, it was theorized that this heat could be utilized elsewhere in the plant. Process models of the oxycombustion boiler, steam cycle, and compressors were created in ASPEN Plus and Excel to test this hypothesis. Using these models, heat from compression stages was integrated to the flue gas recirculation heater, feedwater heaters, and to a fluidized bed coal dryer. All possible combinations of these heat sinks were examined, with improvements in coal flow rate, Qcoal, net power, and unit heat rate being noted. These improvements would help offset the large efficiency impacts inherent to oxycombustion technology.

  5. Experiences with the KEMA Corrosion Probe in waste incineration plants and coal fired boilers

    Energy Technology Data Exchange (ETDEWEB)

    Jong, M.P. de; Leferink, R.G.I. [KEMA Nederland B.V. Arnhem, (Netherlands)

    2001-07-01

    Fireside corrosion is still a major cause of concern in coal- fired power plants and municipal waste incineration plants. In a highly competitive electricity market, the demand for a method to determine the quality or protectiveness of the oxide layers on evaporator walls, in boilers of power plants with low-NO{sub x} firing techniques, will increase. Moreover, co-firing of new fuels (RDF, pulverised wood and other residual fractions) has as yet unknown consequences for corrosion in evaporator walls and super heaters in boiler installations and waste incinerators. Corrosion monitoring enables operators of coal fired power plants to measure and act when corrosion problems are likely to occur. If done properly corrosion monitoring allows the plant operator to adjust the (co-) firing conditions to less corrosive conditions with the highest possible plant efficiency. Recently KEMA developed the KEMA Corrosion Probe (KEMCOP) which enables plant owners to determine fireside corrosion in different locations in their boiler. A good example is the 540 MWe E.on Maasvlakte power plant, which was recently fitted for the exposure of 144 probes simultaneously. The probes can also be used for material testing by exposing different materials under actual firing conditions. Aside from corrosion monitoring also slagging behaviour and condensation of heavy metals can be monitored. In the Netherlands KEMCOP probes are used for several purposes and are more and more becoming common practice for coal fired boilers and waste incinerators. Until now almost 300 probes have been mounted in coal fired boilers and waste incineration plants. (orig.)

  6. Ignition and Combustion of Pulverized Coal and Biomass under Different Oxy-fuel O2/N2 and O2/CO2 Environments

    Science.gov (United States)

    Khatami Firoozabadi, Seyed Reza

    This work studied the ignition and combustion of burning pulverized coals and biomasses particles under either conventional combustion in air or oxy-fuel combustion conditions. Oxy-fuel combustion is a 'clean-coal' process that takes place in O2/CO2 environments, which are achieved by removing nitrogen from the intake gases and recirculating large amounts of flue gases to the boiler. Removal of nitrogen from the combustion gases generates a high CO2-content, sequestration-ready gas at the boiler effluent. Flue gas recirculation moderates the high temperatures caused by the elevated oxygen partial pressure in the boiler. In this study, combustion of the fuels took place in a laboratory laminar-flow drop-tube furnace (DTF), electrically-heated to 1400 K, in environments containing various mole fractions of oxygen in either nitrogen or carbon-dioxide background gases. The experiments were conducted at two different gas conditions inside the furnace: (a) quiescent gas condition (i.e., no flow or inactive flow) and, (b) an active gas flow condition in both the injector and furnace. Eight coals from different ranks (anthracite, semi-snthracite, three bituminous, subbituminous and two lignites) and four biomasses from different sources were utilized in this work to study the ignition and combustion characteristics of solid fuels in O2/N2 or O2/CO2 environments. The main objective is to study the effect of replacing background N2 with CO2, increasing O2 mole fraction and fuel type and rank on a number of qualitative and quantitative parameters such as ignition/combustion mode, ignition temperature, ignition delay time, combustion temperatures, burnout times and envelope flame soot volume fractions. Regarding ignition, in the quiescent gas condition, bituminous and sub-bituminous coal particles experienced homogeneous ignition in both O2/N 2 and O2/CO2 atmospheres, while in the active gas flow condition, heterogeneous ignition was evident in O2/CO 2. Anthracite, semi

  7. Ash transformation in suspension fired boilers co-firing coal and straw

    DEFF Research Database (Denmark)

    Zheng, Yuanjing; Jensen, Peter Arendt; Jensen, Anker Degn

    of flue gas cleaning equipment. This survey includes discussions on the inorganic constituents transformation during straw and coal combustion, alkali-ash and alkali sulfur reactions, a survey of power plant and test rig co-firing experiments, a discussion of equilibrium calculations, a discussion......In this literature report is provided a status for the present knowledge level on ash properties when co-firing coal and biomass. The fly ash formed in boilers using co-firing of coal and straw do have a large influence on ash deposit formation, boiler corrosion, fly ash utilization and operation...... of alkali getter experiments and a discussion of modeling of alkali reaction with kaolin. Presently there is still a need for a better understanding of especially the reaction of potassium with coal ash, thereby making better predictions of co-firing ash properties....

  8. The Simulation of Influence of Different Coals on the Circulating Fluidized Bed Boiler's Combustion Performance

    Institute of Scientific and Technical Information of China (English)

    Yumei Yong; Qinggang Lu

    2003-01-01

    The combustion performance of the boiler largely depends on the coal type. Lots of experimental research shows that different fuels have different combustion characteristics. It is obvious that fuel will change the whole operating performance of Circulating Fluidized Bed Combustion (CFBC). We know even in a pilot-scale running boiler, the measurement of some parameters is difficult and costly. Therefore, we developed the way of simulation to evaluate the combustion performance of Chinese coals in CFB. The simulation results show that,different coals will result in different coal particle diameter and comminution depending on their mineral component and the change will affect the distribution of ash in CFBC system. In a word, the computational results are in accordance with experimental results qualitatively but there are some differences quantitatively.

  9. Mass spectra features of biomass burning boiler and coal burning boiler emitted particles by single particle aerosol mass spectrometer.

    Science.gov (United States)

    Xu, Jiao; Li, Mei; Shi, Guoliang; Wang, Haiting; Ma, Xian; Wu, Jianhui; Shi, Xurong; Feng, Yinchang

    2017-11-15

    In this study, single particle mass spectra signatures of both coal burning boiler and biomass burning boiler emitted particles were studied. Particle samples were suspended in clean Resuspension Chamber, and analyzed by ELPI and SPAMS simultaneously. The size distribution of BBB (biomass burning boiler sample) and CBB (coal burning boiler sample) are different, as BBB peaks at smaller size, and CBB peaks at larger size. Mass spectra signatures of two samples were studied by analyzing the average mass spectrum of each particle cluster extracted by ART-2a in different size ranges. In conclusion, BBB sample mostly consists of OC and EC containing particles, and a small fraction of K-rich particles in the size range of 0.2-0.5μm. In 0.5-1.0μm, BBB sample consists of EC, OC, K-rich and Al_Silicate containing particles; CBB sample consists of EC, ECOC containing particles, while Al_Silicate (including Al_Ca_Ti_Silicate, Al_Ti_Silicate, Al_Silicate) containing particles got higher fractions as size increase. The similarity of single particle mass spectrum signatures between two samples were studied by analyzing the dot product, results indicated that part of the single particle mass spectra of two samples in the same size range are similar, which bring challenge to the future source apportionment activity by using single particle aerosol mass spectrometer. Results of this study will provide physicochemical information of important sources which contribute to particle pollution, and will support source apportionment activities. Copyright © 2017. Published by Elsevier B.V.

  10. Engineering development of advanced coal-fired low-emission boiler systems: Technical progress report No. 16, July-September 1996

    Energy Technology Data Exchange (ETDEWEB)

    Barcikowski, G.F.; Borio, R.W.; Bozzuto, C.R.; Burr, D.H.; Cellilli, L.; Fox, J.D.; Gibbons, T.B.; Hargrove, M.J.; Jukkola, G.D.; King, A.M.

    1996-11-27

    The overall objective of the Project is the expedited commercialization of advanced coal-fired low-emission boiler systems. The Project is under budget and generally on schedule. The current status is shown in the Milestone Schedule Status Report included as Appendix A. Under Task 7--Component development and optimization, the CeraMem filter testing was completed. Due to an unacceptably high flue gas draft loss, which will not be resolved in the POCTF timeframe, a decision was made to change the design of the flue gas cleaning system from Hot SNO{sub x}{sup {trademark}} to an advanced dry scrubber called New Integrated Desulfurization (NID). However, it is recognized that the CeraMem filter still has the potential to be viable in pulverized coal systems. In Task 8-- Preliminary POCTF design, integrating and optimizing the performance and design of the boiler, turbine/generator and heat exchangers of the Kalina cycle as well as the balance of plant design were completed. Licensing activities continued. A NID system was substituted for the SNO{sub x} Hot Process.

  11. Revised users manual, Pulverized Coal Gasification or Combustion: 2-dimensional (87-PCGC-2): Final report, Volume 2. [87-PCGC-2

    Energy Technology Data Exchange (ETDEWEB)

    Smith, P.J.; Smoot, L.D.; Brewster, B.S.

    1987-12-01

    A two-dimensional, steady-state model for describing a variety of reactive and non-reactive flows, including pulverized coal combustion and gasification, is presented. Recent code revisions and additions are described. The model, referred to as 87-PCGC-2, is applicable to cylindrical axi-symmetric systems. Turbulence is accounted for in both the fluid mechanics equations and the combustion scheme. Radiation from gases, walls, and particles is taken into account using either a flux method or discrete ordinates method. The particle phase is modeled in a Lagrangian framework, such that mean paths of particle groups are followed. Several multi-step coal devolatilization schemes are included along with a heterogeneous reaction scheme that allows for both diffusion and chemical reaction. Major gas-phase reactions are modeled assuming local instantaneous equilibrium, and thus the reaction rates are limited by the turbulent rate mixing. A NO/sub x/ finite rate chemistry submodel is included which integrates chemical kinetics and the statistics of the turbulence. The gas phase is described by elliptic partial differential equations that are solved by an iterative line-by-line technique. Under-relaxation is used to achieve numerical stability. The generalized nature of the model allows for calculation of isothermal fluid mechanicsgaseous combustion, droplet combustion, particulate combustion and various mixtures of the above, including combustion of coal-water and coal-oil slurries. Both combustion and gasification environments are permissible. User information and theory are presented, along with sample problems. 106 refs.

  12. NOx EMISSIONS PRODUCED WITH COMBUSTION OF POWDER RIVER BASIN COAL IN A UTILITY BOILER

    Energy Technology Data Exchange (ETDEWEB)

    John S. Nordin; Norman W. Merriam

    1997-04-01

    The objective of this report is to estimate the NOx emissions produced when Powder River Basin (PRB) coal is combusted in a utility boiler. The Clean Air Act regulations specify NOx limits of 0.45 lb/mm Btu (Phase I) and 0.40 lb/mm Btu (Phase II) for tangentially fired boilers, and 0.50 lb/mm 13tu (Phase II) and 0.46 lb/mm Btu (Phase II) for dry-bottom wall-fired boilers. The Clean Air Act regulations also specify other limits for other boiler types. Compliance for Phase I has been in effect since January 1, 1996. Compliance for Phase II goes into effect on January 1, 2000. Emission limits are expressed as equivalent NO{sub 2} even though NO (and sometimes N{sub 2}O) is the NOx species emitted during combustion. Regulatory agencies usually set even lower NOx emission limits in ozone nonattainment areas. In preparing this report, Western Research Institute (WRI) used published test results from utilities burning various coals, including PRB coal, using state-of-the art control technology for minimizing NOx emissions. Many utilities can meet Clean Air Act NOx emission limits using a combination of tight combustion control and low-NOx burners and by keeping furnaces clean (i.e., no slag buildup). In meeting these limits, some utilities also report problems such as increased carbon in their fly ash and excessive furnace tube corrosion. This report discusses utility experience. The theory of NOx emission formation during coal combustion as related to coal structure and how the coal is combusted is also discussed. From this understanding, projections are made for NOx emissions when processed PRB coal is combusted in a test similar to that done with other coals. As will be shown, there are a lot of conditions for achieving low NOx emissions, such as tight combustion control and frequent waterlancing of the furnace to avoid buildup of deposits.

  13. Comparative Techno-economic assessment of biomass and coal with CCS technologies in a pulverized combustion power plant in the United Kingdom

    OpenAIRE

    Al-Qayim, K.; Nimmo, W.; Pourkashanian, M

    2015-01-01

    The technical performance and cost effectiveness of white wood pellets (WWP) combustion in comparison to three types of coal namely U.S., Russian and Colombian coals are investigated in this study. Post-combustion capture and storage (CCS) namely with amine FG+, and oxy-fuel with carbon capture and storage (oxy-fuel) are applied to a 650 MW pulverized combustion (PC) plant. The impacts of the Renewable Obligation Certificate (ROC) and carbon price (CP) policy in accelerating the CCS deploymen...

  14. Coal-fired boiler houses in Cracow present state and possibilities to improve their efficiency

    Energy Technology Data Exchange (ETDEWEB)

    Cyklis, P. [Institute of Industrial Equipment and Power Engineering, Cracow (Poland); Butcher, T.A. [Brookhaven National Lab., Upton, NY (United States)

    1995-12-31

    A significant amount of heat energy both for heating and process purposes is generated in Cracow, Poland in small-and medium size local boiler houses. The operating procedure of these boiler houses is most often economically and ecologically ineffective because of the bad condition of boilers and lack of funds to install automation, control and measurement equipment. Within the Polish-American Program of Elimination of Low Emission Sources financed by the US Department of Energy, the ENERGOEKSPERT Co., Ltd. investigated chosen boiler houses in Cracow, commissioned by the Cracow Development Office. The results of these investigations were subject of engineering analysis carried out at the Institute of Industrial Equipment and Power Engineering, Technical University, Cracow. The analysis proved that the low-cost improvement of economic efficiency and reduction of air pollutant emission is feasible for combustion of coal fuels.

  15. NO{sub x} controls for coal-fired utility boilers in East Central Europe

    Energy Technology Data Exchange (ETDEWEB)

    Eskinazi, D. [Electric Power Research Inst., Washington, DC (United States); Tavoulareas, E.S. [Energy Technologies Enterprises Corp., McLean, VA (United States)

    1995-12-01

    Increasing environmental pressures worldwide, including East Central Europe are placing greater emphasis on NO{sub x} emission controls in utility power plants. Western Europe, Japan and the U.S. have significant experience in applying NO{sub x} controls, especially in boilers firing hard coal. Some countries in Europe (i.e., Germany and Austria), have gained experience in applying NO{sub x} controls in boilers firing low-rank coal. This experience can be applied to East Central European countries in providing the basis for planning NO{sub x} control projects, suggesting cost-effective solutions, and providing lessons learned. However, while the experience is generally applicable to East Central European countries, differences in boiler design, operation and coal characteristics also need to be considered. This paper begins with a comparison of the NO{sub x} regulations, identifies the key NO{sub x} control technologies and the worldwide experience with them, and discusses the achievable NO{sub x} reduction, O&M impacts, and retrofit costs for each technology. Emphasis is placed on retrofit applications for existing boilers, because new coal-fired power plants are not expected to be built for the next 5-10 years. This paper also focuses on technologies with relatively low cost and operational simplicity: combustion system tuning/optimization. low-NO{sub x} burners (LNB), overfire air (OFA), selective non-catalytic reduction (SNCR), and reburning.

  16. INTRODUCTION TO INCONEL ALLOY 740: AN ALLOY DESIGNED FOR SUPERHEATER TUBING IN COAL-FIRED ULTRA SUPERCRITICAL BOILERS

    Institute of Scientific and Technical Information of China (English)

    S.J. Patel

    2005-01-01

    Chinese utilities as well as those worldwide are facingincreased demand for additional electric-ity, reduced plant emissions and greater efficiency.To meet this challenge willrequire increas-ing boiler temperature,pressure and coal ashcorrosion resistance of the materials of boiler construction of future coal-fired boilers. A new nickel-based tube alloy, INCONELRalloy 740,is described aiming at meeting this challenge. Emphasis will be on describing the alloy s mechanical properties, coal-ash and steam corrosion resistance.Microstructural stability as a function of temperature and time is addressed as well as some of the early methodology employed to arrive at the current chemical composition.

  17. Assessment of pulverized-coal-fired combustion performance: Final report for the period September 1980--September 1983

    Energy Technology Data Exchange (ETDEWEB)

    Richter, W.F.; Clark, W.; Pohl, J.H.; Payne, R.

    1987-06-01

    The purpose of this program was to evaluate an engineering analysis procedure which could be used to assess the impact on thermal performance of converting gas and oil fired equipment to coal. The program consisted of four major tasks: (1) Engineering Analysis. The objective was to evaluate currently available models which could be used to predict combustor performance and to define a procedure which could be used to assess the impact of a coal firing in a boiler or furnace; (2) Reactor Studies. The purpose was to evaluate, under controlled conditions, the radiative properties of fly ash clouds; (3) Pilot Scale Experiments. This involved a combustion trial with gas and coals which were burned at 0.7 /times/ 10/sup 6/ Btu/hr in a pilot-scale combustor. The purpose was to verify and supplement the results of the small-scale reactor studies on the radiant properties of coal flames at larger scale; (4) Reporting. Engineering analysis procedures were used to identify those fuels related properties which had a major impact on the thermal performance of furnaces. The major result of the study is that thermal performance of coal-fired furnaces is dominated by the formation of fly ash deposits on the heat transfer surfaces. The key parameters which influence thermal performance are: thickness, thermal conductivity, and surface emissivity or absorptivity. 105 refs., 170 figs., 29 tabs.

  18. Pulverized coal injection at BF N5 during campaign extension period : ArcelorMittal South Africa, Newcastle Works

    Energy Technology Data Exchange (ETDEWEB)

    Scholtz, V. [ArcelorMittal South Africa, Newcastle, KwaZulu-Natal (South Africa)

    2008-07-01

    Blast furnace no. 5 at ArcelorMittal South Africa's Newcastle facility was constructed in 1976 and designed to produce 5000 thm/day, with a hearth diameter of 10.14 m and a working volume of 2017 m{sup 3}. In April 2005, it began using pulverized coal (PC) following a planned maintenance shutdown. Initially, the PC was injected at a rate of 70 kg/thm, but within 5 months, the PC injection (PCI) rate was increased to 160 kg/thm. This was achieved with good replacement ratios, despite a burden that consisted of 40 per cent lump ore. However, the success was brief because of the high rate of unprepared burden, inadequate raw material quality and an aging hearth. The coke rate was therefore increased to reduce hearth wear while maintaining decent hot metal production, resulting in a lower than expected PCI rate of 100 kg/thm. The injection coal rate of 160 kg/thm will be targeted again once the hearth is replaced. Very few changes had been made in the PCI blend in the past because of the low-cost local supply of high volatile, medium ash coals. However, a new coal mine that opened in Newcastle in July 2007 made it possible to partially replace the coal in use. This paper described the operating parameters for the campaign extension period, which required a less than standard injection practice to reduce the amount of production outages. The hearth and stave conditions during the campaign extension were found to be the major barriers to injecting high PCI rates. It was concluded that it is important to re-evaluate the raw material cost for all the fuels used on a regular basis, since the costs to produce coke for higher injection rates could outweigh the advantages at the blast furnace. 3 refs., 1 tabs., 3 figs.

  19. Study of flame combustion of off-design binary coal blends in steam boilers

    Science.gov (United States)

    Kapustyanskii, A. A.

    2017-07-01

    Changes in the structure of the fuel consumption by the thermal power stations of Ukraine caused by failure in supplying anthracite from the Donets Basin are analyzed and the major tasks of maintaining the functioning of the coal industry are formulated. The possibility of using, in the near future, the flame combustion of off-design solid fuels in the power boilers of the thermal power plants and combined heat and power plants is studied. The article presents results of expert tests of the TPP-210A and TP-15 boilers under flame combustion of mixtures of anthracites, lean coal, and the coal from the RSA in various combinations. When combusting, such mixtures have higher values of the combustibles yield and the ash fusibility temperature. The existence of the synergetic effect in the flame combustion of binary coal blends with different degrees of metamorphism is discussed. A number of top-priority measures have been worked out that allow for switching over the boilers designed to be fired with anthracite to using blends of coals of different ranks. Zoned thermal analysis of the TP-15 boiler furnace was performed for numerical investigation of the temperature distribution between the furnace chamber zones and exploration of the possibility of the liquid slag disposal and the temperature conditions for realization of this process. A positive result was achieved by combusting anthracite culm (AC), the coal from the RSA, and their mixtures with lean coal within the entire range of the working loads of the boilers in question. The problems of normalization of the liquid slag flow were also successfully solved without closing the slag notch. The results obtained by balance experiments suggest that the characteristics of the flame combustion of a binary blend, i.e., the temperature conditions in the furnace, the support flame values, and the degree of the fuel burnout, are similar to the characteristics of the flame of the coal with a higher reactive capacity, which

  20. Characterization of Oxy-combustion Impacts in Existing Coal-fired Boilers

    Energy Technology Data Exchange (ETDEWEB)

    Adams, Bradley R. [Univ. of Utah, Salt Lake City, UT (United States); Fry, Andrew R. [Univ. of Utah, Salt Lake City, UT (United States); Senior, Constance L. [Univ. of Utah, Salt Lake City, UT (United States); Shim, Hong Shig [Univ. of Utah, Salt Lake City, UT (United States); Otten, Brydger Van [Univ. of Utah, Salt Lake City, UT (United States); Wendt, Jost [Univ. of Utah, Salt Lake City, UT (United States); Shaddix, Christopher [Sandia National Lab. (SNL-NM), Albuquerque, NM (United States); Tree, Dale [Brigham Young Univ., Provo, UT (United States)

    2010-06-01

    This report summarizes Year 2 results of a research program designed to use multi-scale experimental studies and fundamental theoretical models to characterize and predict the impacts of retrofit of existing coal-fired utility boilers for oxy-combustion. Year 2 focused extensively on obtaining experimental data from the bench-scale, lab-scale and pilot-scale reactors. These data will be used to refine and validate submodels to be implemented in CFD simulations of full-scale boiler retrofits. Program tasks are on schedule for Year 3 completion. Both Year 2 milestones were completed on schedule and within budget.

  1. Neural network approach to the diagnosis of the boiler combustion in a coal power plant

    Energy Technology Data Exchange (ETDEWEB)

    Munoz, A.; Villar, J.; Sanz-Bobi, M.A. [Universidad Pontificia Comillas, Madrid (Spain). Instituto de Investigacion Tecnologia

    1995-08-01

    In order to optimise boiler operation some sort of monitoring system is needed. Monitors can tell the operator about heat production and inputs to heat production; however they cannot monitor the process itself, only its effects. In this example the coal quality used varied, causing the amount of heat produced from the same fuel input to vary. Where quality is very poor the boiler may shutdown. To improve monitoring, flame visualisation techniques were used linked to an automatic diagnosis system. The system was based on artificial neural networks and mathematical techniques. It was installed in the Meirama power plant in Northwest Spain. 18 refs., 17 figs.

  2. Novel fragmentation model for pulverized coal particles gasification in low temperature air thermal plasma

    OpenAIRE

    Jovanović Rastko D.; Cvetinović Dejan B.; Stefanović Predrag Lj.; Škobalj Predrag D.; Marković Zoran J.

    2016-01-01

    New system for start-up and flame support based on coal gasification by low temperature air thermal plasma is planned to supplement current heavy oil system in Serbian thermal power plants in order to decrease air pollutions emission and operational costs. Locally introduced plasma thermal energy heats up and ignites entrained coal particles, thus starting chain process which releases heat energy from gasified coal particles inside burner channel. Important...

  3. Ceramic membrane filters for fine particulate removal in coal-fired industrial boilers

    Energy Technology Data Exchange (ETDEWEB)

    Miller, B.G.; Wincek, R.T.; Glick, D.C.; Scaroni, A.W.; Makris, P.; Krecker, J.; Jung, G.; Stubblefield, D.J.

    1998-07-01

    Strategies are being developed at Penn Sate to produce ultralow emissions when firing coal-based fuel, i.e., micronized coal and coal-water slurry fuel (CWSF), in industrial boilers. The research is being conducted at the bench, pilot, and demonstration scale, and the emissions being addressed are SO{sub 2}, NO{sub x}, fine particulate matter (PM{sub 10} and PM{sub 2.5}), and air toxics (trace elements and volatile organic compounds). Specific activities are identifying/developing a low-temperature NO{sub x} reduction catalyst, studying the occurrence of nitrogen in coal and the fundamental mechanisms of NO{sub x} production, characterizing air toxic emissions, investigating the use of BioLime{trademark} for simultaneous SO{sub 2}/NO{sub x} reduction, and evaluating a ceramic filter for fine particulate control. Results from trace element and polynuclear aromatic hydrocarbon emissions testing when firing coal-based fuels are reported elsewhere in these proceedings. This paper discusses the preliminary results obtained using ceramic membrane filters for fine particulate removal when firing micronized coal in a package boiler.

  4. Combustion of wet pulverized coal in reactor flow; Combustao de particulas de carvao pulverizado contendo umidade em seu interior

    Energy Technology Data Exchange (ETDEWEB)

    Costa, Valdeci Jose [Universidade do Planalto Catarinense (UNIPLAC), Lages, SC (Brazil). Dept. de Ciencias Exatas e Tecnologicas]. E-mail: vcosta@iscc.com.br; Krioukov, Viktor [Universidade Regional do Estado do Rio Grande do Sul (UNIJUI), Ijui, RS (Brazil). Programa de Pos-Graduacao em Modelagem Matematica]. E-mail: krioukov@main.unijui.tche.br; Maliska, Clovis Raimundo [Santa Catarina Univ., Florianopolis, SC (Brazil). Dept. de Engenharia Mecanica]. E-mail: maliska@sinmec.ufsc.br

    2000-07-01

    In this work I propose a numeric study destined to the combustion of wet pulverized coal in reacting flow. The mathematical model is composed by equations for the concentration of the substances in the reacting flow, written based in the chemical kinetics and exponential form, conservation equations and devolatilization equations, combustion of the carbon and residues. The study detects fluctuation among the temperatures of the gas and of the particles. The inclusion of the humidity as constituent part of the volatile matter doesn't affect the performance of the model, however, its presence alters the temperature profiles and the gaseous composition. With the increase of the humidity in the coal have a slight reduction in the time of combustion of the particle, what agrees with experimental data. The model foresees an increment in the difference Tp-Tg and a smaller production of CO with the increase of the wetness rate. The volatile ones, in spite of they have its fraction relatively reduced with the wetness presence they are liberated more slowly with its increment, provoking change in the position of front flame. (author)

  5. Reducing the cost of post combustion capture technology for pulverized coal power plants by flexible operation

    NARCIS (Netherlands)

    Kler, R.C.F. de; Verbaan, M.; Goetheer, E.L.V.

    2013-01-01

    Currently the low carbon prices, low Spreads and regulatory uncertainties hampers the business cases for coal-fired power plants with post-combustion capture (PCC) in Europe. Improvement of the business case of coal-fired power plants with post combustion capture requires a different approach in

  6. Reducing the cost of Post Combustion Capture technology for Pulverized Coal Power Plants by flexible operation

    NARCIS (Netherlands)

    De Kler, R.C.F.; Verbaan, M.; Goetheer, E.L.V.

    2013-01-01

    Currently the low carbon prices, low Spreads and regulatory uncertainties hampers the business cases for coal-fired power plants with post-combustion capture (PCC) in Europe. Improvement of the business case of coal-fired power plants with post combustion capture requires a different approach in

  7. Reducing the cost of Post Combustion Capture technology for Pulverized Coal Power Plants by flexible operation

    NARCIS (Netherlands)

    De Kler, R.C.F.; Verbaan, M.; Goetheer, E.L.V.

    2013-01-01

    Currently the low carbon prices, low Spreads and regulatory uncertainties hampers the business cases for coal-fired power plants with post-combustion capture (PCC) in Europe. Improvement of the business case of coal-fired power plants with post combustion capture requires a different approach in ter

  8. CO-FIRING COAL, FEEDLOT, AND LITTER BIOMASS (CFB AND LFB) FUELS IN PULVERIZED FUEL AND FIXED BED BURNERS

    Energy Technology Data Exchange (ETDEWEB)

    Kalyan Annamalai; John Sweeten; Saqib Mukhtar; Ben Thien; Gengsheng Wei; Soyuz Priyadarsan

    2002-01-15

    Intensive animal feeding operations create large amounts of animal waste that must be safely disposed of in order to avoid environmental degradation. Cattle feedlots and chicken houses are two examples. In feedlots, cattle are confined to small pens and fed a high calorie grain diet in preparation for slaughter. In chicken houses, thousands of chickens are kept in close proximity. In both of these operations, millions of tons of manure are produced every year. In this project a co-firing technology is proposed which would use manure that cannot be used for fertilizer, for power generation. Since the animal manure has economic uses as both a fertilizer and as a fuel, it is properly referred to as feedlot biomass (FB) for cow manure, or litter biomass (LB) for chicken manure. The biomass will be used a as a fuel by mixing it with coal in a 90:10 blend and firing it in existing coal fired combustion devices. This technique is known as co-firing, and the high temperatures produced by the coal will allow the biomass to be completely combusted. Therefore, it is the goal of the current research to develop an animal biomass cofiring technology. A cofiring technology is being developed by performing: (1) studies on fundamental fuel characteristics, (2) small scale boiler burner experiments, (3) gasifier experiments, (4) computer simulations, and (5) an economic analysis. The fundamental fuel studies reveal that biomass is not as high a quality fuel as coal. The biomass fuels are higher in ash, higher in moisture, higher in nitrogen and sulfur (which can cause air pollution), and lower in heat content than coal. Additionally, experiments indicate that the biomass fuels have higher gas content, release gases more readily than coal, and less homogeneous. Small-scale boiler experiments revealed that the biomass blends can be successfully fired, and NO{sub x} pollutant emissions produced will be similar to or lower than pollutant emissions when firing coal. This is a surprising

  9. Experiments and computational modeling of pulverized-coal ignition. Semiannual report, Apr 1, 1998--Sep 30, 1998

    Energy Technology Data Exchange (ETDEWEB)

    John C. Chen; Samuel Owusu-Ofori

    1998-10-31

    Under typical conditions of pulverized-coal combustion, which is characterized by fine particles heated at very high rates, there is currently a lack of certainty regarding the ignition mechanism of bituminous and lower rank coals. It is unclear whether ignition occurs first at the particle-oxygen interface (heterogeneous ignition) or if it occurs in the gas phase due to ignition of the devolatilization products (homogeneous ignition). Furthermore, there have been no previous studies aimed at determining the dependence of the ignition mechanism on variations in experimental conditions, such as particle size, oxygen concentration, and heating rate. Finally, there is a need to improve current mathematical models of ignition to realistically and accurately depict the particle-to-particle variations that exist within a coal sample. Such a model is needed to extract useful reaction parameters from ignition studies, and to interpret ignition data in a more meaningful way. The authors propose to examine fundamental aspects of coal ignition through (1) experiments to determine the ignition mechanism of various coals by direct observation, and (2) modeling of the ignition process to derive rate constants and to provide a more insightful interpretation of data from ignition experiments. They propose to use a novel laser-based ignition experiment to achieve their objectives. The heating source will be a pulsed, carbon dioxide laser in which both the pulse energy and pulse duration are independently variable, allowing for a wide range of heating rates and particle temperatures--both of which are decoupled from each other and from the particle size. This level of control over the experimental conditions is truly novel in ignition and combustion experiments. Laser-ignition experiments also offer the distinct advantage of easy optical access to the particles because of the absence of a furnace or radiating walls, and thus permit direct observation and particle temperature

  10. 论路用混凝土掺合料——粉煤灰%Road Mixes the Material with the Concretes Pulverized Coal Ash

    Institute of Scientific and Technical Information of China (English)

    李吉平

    2009-01-01

    This paper introduced the road mixes the material pulverized coal ash with the concretes the characteristic, technical performance, to pulverized coal ash quality requirement, standard, choice, design requirements and isometric substitution law and excess substitution method com-putation principle.%文章介绍了路用混凝土掺合料粉煤灰的特点、技术性能、对粉煤灰的质量要求、标准、选择,以及设计要求和配制混凝土时取代水泥的等量取代法和超量取代法的计算原理.

  11. An annular-furnace boiler for the 660-MW power unit for ultrasupercritical parameters intended for firing brown slagging coals

    Science.gov (United States)

    Serant, F. A.; Belorutskii, I. Yu.; Ershov, Yu. A.; Gordeev, V. V.; Stavskaya, O. I.; Katsel, T. V.

    2013-12-01

    We present the main technical solutions adopted in designing annular-furnace boilers intended for operation on brown coals of the prospective Maikubensk open-cast mine in Kazakhstan as part of 660-MW power units for ultrasupercritical steam conditions. Results from 3D modeling of combustion processes are presented, which clearly show the advantages furnaces of this kind have over a traditional furnace in burning heavily slagging brown coals. The layout of the main and boiler auxiliary equipment in the existing boiler cell of the 500-MW power unit at the Ekibastuz GRES-1 district power station is shown. Appropriate attention is paid to matters concerned with decreasing harmful emissions.

  12. Sliding Mode Predictive Control of Main Steam Pressure in Coal-fired Power Plant Boiler

    Institute of Scientific and Technical Information of China (English)

    史元浩; 王景成; 章云锋

    2012-01-01

    Since the combustion system of coal-fired boiler in thermal power plant is characterized as time varying, strongly coupled, and nonlinear, it is hard to achieve a satisfactory performance by the conventional proportional integral derivative (PID) control scheme. For the characteristics of the main steam pressure in coal-fired power plant boiler, the sliding mode control system with Smith predictive structure is proposed to look for performance and robustness improvement. First, internal model control (IMC) and Smith predictor (SP) is used to deal with the time delay, and sliding mode controller (SMCr) is designed to overcome the model mismatch. Simulation results show the effectiveness of the proposed controller compared with conventional ones.

  13. 800-MW Supercritical Coal-Fired Boilers in Suizhong Power Plant

    Institute of Scientific and Technical Information of China (English)

    Zou Haifeng; Li Zhishan; Liu Zhongqi; Yan Hongyong; Zhang Yuanliang; Wang Lei

    2005-01-01

    This article reviews the problems of Russia-made 800-MW coal-fired supercritical boilers inSuizhong Power Plant, such as burner burnout, water-wall leakage, slag screen I explosion, crack happenedon the desuperheater outlet of reheater and welding defect of economizer; tells the process of renovating theseunits by modifying the original design and adjusting the operation parameters. After several years' effort, allthe problems have been well solved. The experience may be useful for other imported units in China.

  14. Chemical and toxicological characterization of organic constituents in fluidized-bed and pulverized coal combustion: a topical report

    Energy Technology Data Exchange (ETDEWEB)

    Chess, E.K.; Later, D.W.; Wilson, B.W.; Harris, W.R.; Remsen, J.F.

    1984-04-01

    Coal combustion fly ash from both conventional pulverized coal combustion (PCC) and fluidized-bed combustion (FBC) have been characterized as to their organic constituents and microbial mutagenic activity. The PCC fly ash was collected from a commercial utility generating plant using a low sulfur coal. The FBC fly ash was from a bench-scale developmental unit at the Grand Forks Energy Technology Center. Bulk samples of each fly ash were extracted using benzene/methanol and further separated using high performance liquid chromatography (HPLC). Subfractions from the HPLC separation were analyzed by gas chromatography using both element-specific nitrogen-phosphorus detectors and flame ionization detectors. Microbial mutagenicity assay results indicated that the crude organic extracts were mutagenic, and that both the specific activity and the overall activity of the PCC material was greater than that of the FBC material. Comparison of results from assays using S. typhimurium, TA1538NR indicated that nitrated polycyclic aromatic compounds (PAC) were responsible for much of the mutagenic activity of the PCC material. Similar results were obtained for assays of the FBC organic extract with standard and nitroreductase-deficient strains of S. typhimurium, TA100 and TA1538. Mutagenically active HPLC fractions were analyzed using high resolution gas chromatography (HRGC) and GC mass spectrometry (GC/MS), as well as probe inlet low and high resolutions MS. The discovery and identification of nitrated, oxygenated PAC are important because the presence of both nitro and/or keto functionalities on certain PAC has been shown to confer or enhance mutagenic activity.

  15. Ash transformation in suspension fired boilers co-firing coal and straw

    DEFF Research Database (Denmark)

    Zheng, Yuanjing; Jensen, Peter Arendt; Jensen, Anker Degn;

    The properties of the ash from co-firing of coal and straw have a large influence on boiler operation, flue gas cleaning equipment and appropriate utilization of the fly ash. A study on the fuel composition and local conditions influence on fly ash properties has been done by making entrained flow...... reactor experiments with co-firing of coal and straw, making mineral and alkali vapor laboratory reactor experiments and by developing a model of KCl reaction with kaolin. The results include correlations that can be used to estimate the speciation of potassium in the fly ash when co-firing straw...

  16. Influence of rank and macerals on the burnout behaviour of pulverized Indian coal

    Energy Technology Data Exchange (ETDEWEB)

    Choudhury, Nandita; Biswas, S.; Sarkar, P.; Kumar, Manish; Mukherjee, A.; Choudhury, A. [Central Institute of Mining and Fuel Research, Digwadih Campus (Formerly Central Fuel Research Institute), P.O. FRI, Dhanbad-828 108, Jharkhand (India); Ghosal, Sujit; Mitra, Tandra [Jadavpur University, Kolkata-700 032, West Bengal (India)

    2008-04-03

    The combustion behaviour of coal is significantly influenced by its rank and maceral and microlithotype compositions. Different macerals, due to their distinct and unique physical properties and chemical makeup, have different burning characteristics. This paper deals with the burning behaviour of coals of Indian origin by thermo gravimetric analysis (TGA) and in drop tube furnace (DTF) with particular emphasis on the role of macerals and their associations. Four coals of different rank and petrographic makeup, along with their two density fractions, with enriched vitrinite and inertinites, respectively,were studied in both TGA and DTF. The burnout behaviour was estimated from the chemical analyses of the char samples collected from the DTF. The burning characteristics of one of the coals deviate from the trend expected with the variations of rank. The behaviour of the density fractions in DTF was found to be different from that observed in TGA analyses. An attempt has been made to correlate the burnout with the petrographic macerals and microlithotypes present in the coals. The morphology of the residual chars indicates the contributions of the inertinites towards the formation of cenospheres and network types of reactive chars. The superior burning behaviour of the higher density inertinite-rich fractions over the raw coals and also some vitrinite-rich fractions indicate the better reactivity of the inertinites towards combustion. (author)

  17. CFD prediction of physical field for multi-air channel pulverized coal burner in rotary kiln

    Institute of Scientific and Technical Information of China (English)

    2006-01-01

    A 3-D numerical simulation with CFX software on physical field of multi-air channel coal burner in rotary kiln was carried out. The effects of various operational and structural parameters on flame feature and temperature distribution were investigated. A thermal measurement was conducted on a rotary kiln (4.5 m in diameter, 90 m in length) with four-air channel coal burner to determine the boundary conditions and to verify the simulation results.The calculation result shows that the distribution of velocity near burner exit is saddle-like; recirculation zones near nozzle and wall are useful for mixture primary air with coal and high temperature fume. A little central airflow can avoid coal backing up and cool nozzle. Adjusting the ratio of internal airflow to outer airflow is an effective and major means to regulate flame and temperature distribution in sintering region. Large whirlcone angle can intensify disturbution range at flame root to accelerate ignition and mixture. Large coal size can reduce high temperature region and result in coal combusting insufficiently. Too much combustion air will lengthen flame and increase heat loss.

  18. Characterization of Oxy-combustion Impacts in Existing Coal-fired Boilers

    Energy Technology Data Exchange (ETDEWEB)

    Adams, Bradley [Univ. of Utah, Salt Lake City, UT (United States); Davis, Kevin [Univ. of Utah, Salt Lake City, UT (United States); Senior, Constance [Univ. of Utah, Salt Lake City, UT (United States); Shim, Hong Shim [Univ. of Utah, Salt Lake City, UT (United States); Otten, Brydger Van [Univ. of Utah, Salt Lake City, UT (United States); Fry, Andrew [Univ. of Utah, Salt Lake City, UT (United States); Wendt, Jost [Univ. of Utah, Salt Lake City, UT (United States); Eddings, Eric [Univ. of Utah, Salt Lake City, UT (United States); Paschedag, Alan [Sandia National Lab. (SNL-NM), Albuquerque, NM (United States); Shaddix, Christopher [Sandia National Lab. (SNL-NM), Albuquerque, NM (United States); Cox, William [Brigham Young Univ., Provo, UT (United States); Tree, Dale [Brigham Young Univ., Provo, UT (United States)

    2013-09-30

    Reaction Engineering International (REI) managed a team of experts from University of Utah, Siemens Energy, Praxair, Vattenfall AB, Sandia National Laboratories, Brigham Young University (BYU) and Corrosion Management Ltd. to perform multi-scale experiments, coupled with mechanism development, process modeling and CFD modeling, for both applied and fundamental investigations. The primary objective of this program was to acquire data and develop tools to characterize and predict impacts of CO{sub 2} flue gas recycle and burner feed design on flame characteristics (burnout, NO{sub x}, SO{sub x}, mercury and fine particle emissions, heat transfer) and operational concerns (fouling, slagging and corrosion) inherent in the retrofit of existing coal-fired boilers for oxy-coal combustion. Experimental work was conducted at Sandia National Laboratories’ Entrained Flow Reactor, the University of Utah Industrial Combustion Research Facility, and Brigham Young University. Process modeling and computational fluid dynamics (CFD) modeling was performed at REI. Successful completion of the project objectives resulted in the following key deliverables: 1) Multi-scale test data from 0.1 kW bench-scale, 100 kW and 200 kW laboratory-scale, and 1 MW semi-industrial scale combustors that describe differences in flame characteristics, fouling, slagging and corrosion for coal combustion under air-firing and oxygen-firing conditions, including sensitivity to oxy-burner design and flue gas recycle composition. 2) Validated mechanisms developed from test data that describe fouling, slagging, waterwall corrosion, heat transfer, char burnout and sooting under coal oxy-combustion conditions. The mechanisms were presented in a form suitable for inclusion in CFD models or process models. 3) Principles to guide design of pilot-scale and full-scale coal oxy-firing systems and flue gas recycle configurations, such that boiler operational impacts from oxy-combustion retrofits are minimized. 4

  19. Joule II - Programme. Clean coal technology R & D. 2nd phase. Volume III. Atmospheric combustion of pulverized coal and coal based blends for power generation

    Energy Technology Data Exchange (ETDEWEB)

    Hein, K.R.G.; Minchener, A.J.; Pruschek, R.; Roberts, P.A. [eds.

    1998-12-31

    Topics covered in this Joule II clean coal technology publication include: coal preparation and blending; cocombustion of coal with biomass and wastes; flame modelling; NO{sub x} abatement by combustion control and staging; coal quality and NO{sub x} emissions; coal combustion properties; and fluidized bed combustion of coal. All papers have been abstracted separately.

  20. Recovery Act: Oxy-Combustion Technology Development for Industrial-Scale Boiler Applications

    Energy Technology Data Exchange (ETDEWEB)

    Levasseur, Armand

    2014-01-01

    This Topical Report outlines guidelines and key considerations for design and operation of pulverized coal-fired boilers for oxy-combustion. The scope addressed includes only the boiler island, not the entire oxy-fired CO{sub 2} capture plant. These guidelines are primarily developed for tangential-fired boilers and focus on designs capable of dual air and oxy-fired operation. The guidelines and considerations discussed are applicable to both new units and existing boiler retrofits. These guidelines are largely based on the findings from the extensive 15 MW{sub th} pilot testing and design efforts conducted under this project. A summary level description is provided for each major aspect of boiler design impacted by oxy-combustion, and key considerations are discussed for broader application to different utility and industrial designs. Guidelines address the boiler system arrangement, firing system, boiler thermal design, ducting, materials, control system, and other key systems.

  1. Adsorbents for capturing mercury in coal-fired boiler flue gas.

    Science.gov (United States)

    Yang, Hongqun; Xu, Zhenghe; Fan, Maohong; Bland, Alan E; Judkins, Roddie R

    2007-07-19

    This paper reviews recent advances in the research and development of sorbents used to capture mercury from coal-fired utility boiler flue gas. Mercury emissions are the source of serious health concerns. Worldwide mercury emissions from human activities are estimated to be 1000 to 6000 t/annum. Mercury emissions from coal-fired power plants are believed to be the largest source of anthropogenic mercury emissions. Mercury emissions from coal-fired utility boilers vary in total amount and speciation, depending on coal types, boiler operating conditions, and configurations of air pollution control devices (APCDs). The APCDs, such as fabric filter (FF) bag house, electrostatic precipitator (ESP), and wet flue gas desulfurization (FGD), can remove some particulate-bound and oxidized forms of mercury. Elemental mercury often escapes from these devices. Activated carbon injection upstream of a particulate control device has been shown to have the best potential to remove both elemental and oxidized mercury from the flue gas. For this paper, NORIT FGD activated carbon was extensively studied for its mercury adsorption behavior. Results from bench-, pilot- and field-scale studies, mercury adsorption by coal chars, and a case of lignite-burned mercury control were reviewed. Studies of brominated carbon, sulfur-impregnated carbon and chloride-impregnated carbon were also reviewed. Carbon substitutes, such as calcium sorbents, petroleum coke, zeolites and fly ash were analyzed for their mercury-adsorption performance. At this time, brominated activated carbon appears to be the best-performing mercury sorbent. A non-injection regenerable sorbent technology is briefly introduced herein, and the issue of mercury leachability is briefly covered. Future research directions are suggested.

  2. 配煤技术在Shell粉煤气化中的应用及优化%THE APPLICATION AND OPTIMIZATION OF COAL BLENDING IN SHELL PULVERIZED-COAL GASIFICATION PROCESS

    Institute of Scientific and Technical Information of China (English)

    吴国祥

    2012-01-01

    The requirement for coal property on Shell pulverized-coal gasification process is simply introduced and the definition and theoretical foundation of Coal blending technology are described.The main reasons for coal blending measure to Shell coal gasification plant are analyzed and concrete procedures of coal blending technology and corresponding cases are discussed in detail and the optimized measures for coal blending are resulted in.%介绍Shell粉煤气化工艺对煤质的要求,阐述配煤技术的定义及理论依据,分析Shell气化采用配煤措施的主要原因,详细论述配煤技术的具体实施步骤及相应案例,得出优化配煤的措施。

  3. The advanced super critical 700{sup o}C pulverized coal-fired power plant

    Energy Technology Data Exchange (ETDEWEB)

    Kjaer, S.; Klauke, F.; Vanstone, R.; Zeijseink, A.; Weissinger, G.; Kristensen, P.; Meier, J.; Blum, R.; Wieghardt, K. [Tech-Wise A/S, Fredericia (Denmark)

    2001-07-01

    This paper presents the efforts of a large European group of manufacturers, utilities and institutes co-operating in a phased long-term project named 'Advanced 700{sup o}C PF Power Plant'. The first phase started in 1998 based on a grant from the Commission's Thermie programme under the 4th Framework programme. The overall objective of the project is to ensure a role for coal in Europe also in future. The project's targets renewedpublic and political acceptance of coal by improving efficiency and economy of well-proven, super critical pulverised coal-fired technology. Net efficiencies of more than 50% will be reached through development of a super critical steam cycle operating at maximum steam temperatures in the range of 700{sup o}C. Principal efforts are based on development of creep resistant - and expensive - nickel-based materials named super-alloys for the hottest areas of the water/steam cycle. Three benchmarks for theinvestigations have been set up: (i) the net efficiency of the demonstration plant from the present state of the art performance of 44% will be boosted into the range of 50-51% for a plant located inland with a cooling tower and 53-54% for the best seawater-cooled versions. (ii) reductions of investment cost of PF power plant by revising the overall architecture of the plant. (iii) Co-firing of up to 20% biomass with coal. The Advanced 700{sup o}C PF power plant project (or AD700) will improve the competitiveness of coal-fired power generation and give a major reduction of CO{sub 2} from coal-fired power plants in the range of 15% from the best PF power plants presently and up to 40% from older plants. 11 figs., 2 tabs.

  4. FUNDAMENTAL INVESTIGATION OF FUEL TRANSFORMATIONS IN PULVERIZED COAL COMBUSTION AND GASIFICATION TECHNOLOGIES

    Energy Technology Data Exchange (ETDEWEB)

    Robert Hurt; Joseph Calo; Thomas Fletcher; Alan Sayre

    2004-01-01

    The goal of this project is to carry out the necessary experiments and analyses to extend leading submodels of coal transformations to the new conditions anticipated in next-generation energy technologies. During the first two projects years, significant progress was made on most of the tasks, as described in detail in the two previous annual reports. In the current third annual report, we report in detail on the BYU task on the properties and intrinsic reactivities of chars prepared at high-pressure. A flat-flame burner was used in a high pressure laminar flow facility to conduct high temperature, high heating rate coal pyrolysis experiments. Heating rates were approximately 10{sup 5} K/s, which is higher than in conventional drop tube experiments. Char samples from a Pitt No.8 coal and lignite were collected at 1300 C at 1, 6, 10, and 15 atm. Swelling ratios of the lignite were less than 1.0, and only about 1.3 for the Pitt No.8 coal. All coals showed slight increases in swelling behavior as pressure increased. The swelling behavior observed for the Pitt No.8 coal at each pressure was lower than reported in high pressure drop tube experiments, indicating the effect of heating rate on particle swelling. This heating rate effect was similar to that observed previously at atmospheric pressure. SEM photos revealed that bituminous coal has large physical structure transformations, with popped bubbles due to the high heating rate. TGA char oxidation reactivities were measured at the same total pressure as the char preparation pressure. The general trend was that the TGA reactivity on a gram per gram available basis decreased for both Pitt No.8 and Knife River lignite coal chars with increasing char formation pressure. The Pitt No.8 char intrinsic activation energy and oxygen reaction order remained relatively constant with increasing pressure. This new data provides some of the only information available on the morphology, structure, and reactivity of chars prepared in

  5. EFFECT OF HEATING RATE ON THE THERMODYNAMIC PROPERTIES OF PULVERIZED COAL

    Energy Technology Data Exchange (ETDEWEB)

    Ramanathan Sampath

    2000-01-01

    This final technical report describes work performed under DOE Grant No. DE-FG22-96PC96224 during the period September 24, 1996 to September 23, 1999 which covers the entire performance period of the project. During this period, modification, alignment, and calibration of the measurement system, measurement of devolatilization time-scales for single coal particles subjected to a range of heating rates and temperature data at these time-scales, and analysis of the temperature data to understand the effect of heating rates on coal thermal properties were carried out. A new thermodynamic model was developed to predict the heat transfer behavior for single coal particles using one approach based on the analogy for thermal property of polymers. Results of this model suggest that bituminous coal particles behave like polymers during rapid heating on the order of 10{sup 4}-10{sup 5} K/s. At these heating rates during the early stages of heating, the vibrational part of the heat capacity of the coal molecules appears to be still frozen but during the transition from heat-up to devolatilization, the heat capacity appears to attain a sudden jump in its value as in the case of polymers. There are a few data available in the coal literature for low heating rate experiments (10{sup 2}-10{sup 3} K/s) conducted by UTRC, our industrial partner, in this project. These data were obtained for a longer heating duration on the order of several seconds as opposed to the 10 milliseconds heating time of the single particle experiments discussed above. The polymer analogy model was modified to include longer heating time on the order of several seconds to test these data. However, the model failed to predict these low heating rate data. It should be noted that UTRC's work showed reasonably good agreement with Merrick model heat capacity predictions at these low heating rates, but at higher heating rates UTRC observed that coal thermal response was heat flux dependent. It is concluded

  6. Numerical study of bituminous coal combustion in a boiler furnace with bottom blowing

    Science.gov (United States)

    Zroychikov, N. A.; Kaverin, A. A.

    2016-11-01

    Results obtained by the numerical study of a solid fuel combustion scheme with bottom blowing using Ekibastuz and Kuznetsk bituminous coals of different fractional makeup are presented. Furnace chambers with bottom blowing provide high-efficiency combustion of coarse-grain coals with low emissions of nitrogen oxides. Studying such a combustion scheme, identification of its technological capabilities, and its further improvement are topical issues. As the initial object of study, we selected P-57-R boiler plant designed for burning of Ekibastuz bituminous coal in a prismatic furnace with dry-ash (solid slag) removal. The proposed modernization of the furnace involves a staged air inflow under the staggered arrangement of directflow burners (angled down) and bottom blowing. The calculation results revealed the specific aerodynamics of the flue gases, the trajectories of solid particles in the furnace chamber, and the peculiarities of the fuel combustion depending on the grinding fineness. It is shown that, for coal grinding on the mill, the overall residue on the screen plate of 90 µm ( R 90 ≤ 27% for Ekibastuz coal and R 90 ≤ 15% for Kuznetsk coal) represents admissible values for fuel grind coarsening in terms of economic efficiency and functional reliability of a boiler. The increase in these values leads to the excess of regulatory heat losses and unburned combustible losses. It has been established that the change in the grade of the burned coal does not significantly affect the flow pattern of the flue gases, and the particles trajectory is essentially determined by the elemental composition of the fuel.

  7. Risk management of energy efficiency projects in the industry - sample plant for injecting pulverized coal into the blast furnaces

    Directory of Open Access Journals (Sweden)

    Jovanović Filip P.

    2016-01-01

    Full Text Available This paper analyses the applicability of well-known risk management methodologies in energy efficiency projects in the industry. The possibilities of application of the selected risk management methodology are demonstrated within the project of the plants for injecting pulverized coal into blast furnaces nos. 1 and 2, implemented by the company US STEEL SERBIA d.o.o. in Smederevo. The aim of the project was to increase energy efficiency through the reduction of the quantity of coke, whose production requires large amounts of energy, reduction of harmful exhaust emission and increase productivity of blast furnaces through the reduction of production costs. The project was complex and had high costs, so that it was necessary to predict risk events and plan responses to identified risks at an early stage of implementation, in the course of the project design, in order to minimise losses and implement the project in accordance with the defined time and cost limitations. [Projekat Ministarstva nauke Republike Srbije, br. 179081: Researching contemporary tendencies of strategic management using specialized management disciplines in function of competitiveness of Serbian economy

  8. Utilization of blended fluidized bed combustion (FBC) ash and pulverized coal combustion (PCC) fly ash in geopolymer.

    Science.gov (United States)

    Chindaprasirt, Prinya; Rattanasak, Ubolluk

    2010-04-01

    In this paper, synthesis of geopolymer from fluidized bed combustion (FBC) ash and pulverized coal combustion (PCC) fly ash was studied in order to effectively utilize both ashes. FBC-fly ash and bottom ash were inter-ground to three different finenesses. The ashes were mixed with as-received PCC-fly ash in various proportions and used as source material for synthesis of geopolymer. Sodium silicate (Na(2)SiO(3)) and 10M sodium hydroxide (NaOH) solutions at mass ratio of Na(2)SiO(3)/NaOH of 1.5 and curing temperature of 65 degrees C for 48h were used for making geopolymer. X-ray diffraction (XRD), scanning electron microscopy (SEM), degree of reaction, and thermal gravimetric analysis (TGA) were performed on the geopolymer pastes. Compressive strength was also tested on geopolymer mortars. The results show that high strength geopolymer mortars of 35.0-44.0MPa can be produced using mixture of ground FBC ash and as-received PCC-fly ash. Fine FBC ash is more reactive and results in higher degree of reaction and higher strength geopolymer as compared to the use of coarser FBC ash. Grinding increases reactivity of ash by means of increasing surface area and the amount of reactive phase of the ash. In addition, the packing effect due to fine particles also contributed to increase in strength of geopolymers.

  9. The effects of unburned carbon on radiative heat transfer in a pilot pulverized coal furnace -- Numerical investigation

    Energy Technology Data Exchange (ETDEWEB)

    Liu Zhaohui; Xing Huawei; Zhou Yingbiao; Zheng Chuguang [National Lab. of Coal Combustion, Wuhan (China)

    1997-12-31

    This paper investigates the possible effect of residue char on the radiative heat transfer in a pilot furnace. Firstly, a program is constructed to incorporate radiative properties of particles in solving the radiative heat transfer, based on a computer code for predicting turbulent gas-solid flow and combustion. The radiative properties of single unburnt char are modeled by coated sphere model of Mie theory, while the local Planck average radiative properties of particle could be obtained by a scheme based on Lagrangian approach with particle turbulent dispersion, and the radiative heat transfer is solved by Discrete Transfer method. Then, comparisons are made among predicted results for a pilot-scale pulverized coal furnace by several particulate radiative properties models. It shows even for the pilot-scale furnace, the effect of particle concentration is more important than that of distinguishing between particles of char and ash. The residue carbon in ash has a tendency to enhance the radiative heat transfer for this case. The optimized burn-off rate to separate ash from char is near 0.65.

  10. Assessment of ecotoxicological risks of element leaching from pulverized coal ashes

    NARCIS (Netherlands)

    Jenner, H.A.

    1995-01-01

    This thesis describes the consequences of the disposal of the combustion residues of coal, especially the uptake of elements from such residues and their effects on various organisms. The effects on benthic organisms in fresh and in seawater are considered in the first two parts. The third

  11. Temporal trends and spatial variation characteristics of primary air pollutants emissions from coal-fired industrial boilers in Beijing, China.

    Science.gov (United States)

    Xue, Yifeng; Tian, Hezhong; Yan, Jing; Zhou, Zhen; Wang, Junling; Nie, Lei; Pan, Tao; Zhou, Junrui; Hua, Shenbing; Wang, Yong; Wu, Xiaoqing

    2016-06-01

    Coal-fired combustion is recognized as a significant anthropogenic source of atmospheric compounds in Beijing, causing heavy air pollution events and associated deterioration in visibility. Obtaining an accurate understanding of the temporal trends and spatial variation characteristics of emissions from coal-fired industrial combustion is essential for predicting air quality changes and evaluating the effectiveness of current control measures. In this study, an integrated emission inventory of primary air pollutants emitted from coal-fired industrial boilers in Beijing is developed for the period of 2007-2013 using a technology-based approach. Future emission trends are projected through 2030 based on current energy-related and emission control policies. Our analysis shows that there is a general downward trend in primary air pollutants emissions because of the implementation of stricter local emission standards and the promotion by the Beijing municipal government of converting from coal-fired industrial boilers to gas-fired boilers. However, the ratio of coal consumed by industrial boilers to total coal consumption has been increasing, raising concerns about the further improvement of air quality in Beijing. Our estimates indicate that the total emissions of PM10, PM2.5, SO2, NOx, CO and VOCs from coal-fired industrial boilers in Beijing in 2013 are approximately 19,242 t, 13,345 t, 26,615 t, 22,965 t, 63,779 t and 1406 t, respectively. Under the current environmental policies and relevant energy savings and emission control plans, it may be possible to reduce NOx and other air pollutant emissions by 94% and 90% by 2030, respectively, if advanced flue gas purification technologies are implemented and coal is replaced with natural gas in the majority of existing boilers.

  12. Impacts and implementation of fuel moisture release and radiation properties in modelling of pulverized fuel combustion processes

    DEFF Research Database (Denmark)

    Yin, Chungen

    2015-01-01

    Pulverized fuels (PF) prepared and fired in utility boilers usually contain a certain amount of moisture, either free moisture or chemically bound moisture. In PF furnaces, radiation which is the principal mode of heat transfer consists of contribution from both gas and particle phase. This paper...... presents different methods for fuel moisture release and new models for gas and particle radiative properties, and demonstrates their implementation, importance and impacts in PF combustion modelling via a comprehensive CFD study of a pulverized coal-fired utility boiler. To conclude, it is recommended...... to add the free moisture into the primary air stream while lump the moisture retained in the feed after the mills with volatiles in PF combustion modelling. For gas and particle radiation in PF boilers, it is found that particle radiation largely overwhelms gas radiation due to high particle loading...

  13. Duquesne Light Company`s modifications for nitric oxide RACT compliance on a 200 MW face fired pulverized coal unit

    Energy Technology Data Exchange (ETDEWEB)

    Breen, B.P.; Bionda, J.P.; Gabrielson, J.E. [Energy Systems Associates, Pittsburgh, PA (United States); Hallo, A.; Gretz, G.F. [Duquesne Light Co., Pittsburgh, PA (United States)

    1996-12-31

    This paper discusses the results of a research test program conducted on Duquesne Light Company`s Elrama Unit 4. The program was designed to determine the viability of achieving compliance with the recently enacted PA DER Reasonably Available Control Technology (RACT) regulations. These regulations stipulate presumptive RACT requirements for wall fired boilers which include the installation and operation of low NO{sub x} burners with separated overfire air. Duquesne Light Company contracted Energy Systems Associates (ESA) to aide in the design and testing of a novel low NO{sub x} burner design and separated overfire air system. A three-dimensional computational furnace model was developed by ESA of the Elrama Unit 4 furnace, and a two-dimensional fluid dynamics model was developed of the coal burner. By modifying the coal burners, it has been possible to reduce the nitric oxide emissions by 30% on Unit 4, with minimal impact of the unburned carbon in the ash. The burner modifications create fuel rich streams which are surrounded by air rich zones in the primary flame region, thus staging combustion at the burner. Additional nitric oxide reductions are realized when the combustion is further staged by use of the separated overfire air system.

  14. Deposit Formation during Coal-Straw Co-Combustion in a Utility PF-Boiler

    DEFF Research Database (Denmark)

    Andersen, Karin Hedebo

    1998-01-01

    observed, but can not represent the mature deposits satisfactorily. The chemical composition of the mature deposits indicate, that sulphate based consolidation is of importance in the deposit maturation.The chemical elements of primary interest in coal-straw co-combustion are K and Cl, which are both...... introduced with the straw was bonded as K-Al-silicate during combustion, and the remaining available K formed K2SO4, which could participate in deposit formation and consolidation. No significant participation of K was seen in the coal ash deposits, whereas K was a large contributor the up- and downstream.......In conclusion, this study has provided new knowledge on the effects of coal-straw co-combustion on fouling deposit formation in a full-scale PF-boiler, including an experimental and thermodynamic evaluation of the behaviour of elements originating from the straw in deposits and fly ash, and the limits...

  15. Ash transformation in suspension fired boilers co-firing coal and straw

    DEFF Research Database (Denmark)

    Zheng, Yuanjing; Jensen, Peter Arendt; Jensen, Anker Degn

    To study the influence of local conditions on the reaction between gaseous KCl and kaolin or coal fly ash experiments were done on CHECs electrically heated entrained flow reactor, which can simulate the local conditions in suspension fired boilers. The experimental results were compared with model...... (1100-1300 °C) or a changed amount of KCl (K/Si = 0.1 – 0.34) did only change the KCl conversion slightly. Si and Al rich coal ash seems to be less efficient to react with KCl compared to kaolin. However the applied coal ash had a larger particle size (d50 = 22μm) compared to the kaolin (d50 = 10μm)....

  16. An assessment of the environmental emissions from a utility boiler firing beneficiated coal-oil mixtures

    Energy Technology Data Exchange (ETDEWEB)

    Whaley, H,; Lee, L.K.; Doiron, C.C.

    1980-01-01

    A cooperative demonstration project to evaluate the feasibility of burning coal-oil mixtures (COM) in a small utility boiler is described. The project, undertaken by the New Brunswick Electric Power Commission and the Department of Energy, Mines and Resources Canada has, as a mator objective, an assessment of the environmental impact of COM technology and whether this can be reduced through coal cleaning by spherical agglomeration. It is shown that fly ash emissions can be reduced by as much as 50% and sulphur emissions by 10% using the coal cleaning process. Laboratory tests indicate that this performance can be significantly improved. The paper describes the emissions test program and summarises the emissions of fly ash and sulphur from two years of operation both with and without the agglomeration process.

  17. Reduction of Nitrogen Oxides Emissions from a Coal-Fired Boiler Unit

    Directory of Open Access Journals (Sweden)

    Zhuikov Andrey V.

    2016-01-01

    Full Text Available During combustion of fossil fuels a large amount of harmful substances are discharged into the atmospheres of cities by industrial heating boiler houses. The most harmful substances among them are nitrogen oxides. The paper presents one of the most effective technological solutions for suppressing nitrogen oxides; it is arrangement of circulation process with additional mounting of the nozzle directed into the bottom of the ash hopper. When brown high-moisture coals are burnt in the medium power boilers, generally fuel nitrogen oxides are produced. It is possible to reduce their production by two ways: lowering the temperature in the core of the torch or decreasing the excess-air factor in the boiler furnace. Proposed solution includes the arrangement of burning process with additional nozzle installed in the lower part of the ash hopper. Air supply from these nozzles creates vortex involving large unburned fuel particles in multiple circulations. Thereby time of their staying in the combustion zone is prolonging. The findings describe the results of the proposed solution; and recommendations for the use of this technological method are given for other boilers.

  18. Coal selection for NO{sub x} reduction in pulverized fuel combustion

    Energy Technology Data Exchange (ETDEWEB)

    Gibbins, J.R.; Lockwood, F.C.; Man, C.K.; Williamson, J.; Hesselman, G.J.; Downer, B.M.; Skorupska, N.M. [Imperial College of Science, Technology and Medicine, London (United Kingdom)

    1995-12-31

    A major factor affecting a coal`s performance in air-staged low-NO{sub x} burners is the amount of nitrogen remaining in the char after devolatilisation. Current standard proximate devolatilisation tests do not apply realistic heating conditions for PF combustion, but a recently-developed high-temperature wire-mesh reactor now allows relatively simple captive-sample measurements at heating rates of 10{sup 4} K/s. Char nitrogen data is reported for devolatilisation temperatures from 400{degree}C to 1800{degree}C, including values for a range of UK and world-traded coals for which NO{sub x} measurements from three full-scale low-NO{sub x} utility plants and/or a pilot combustor are available. The most general correlation between char nitrogen and combustion NO{sub x} is observed for a peak preparation temperature of 1800{degree}C with 0.15 s (or 2 s) hold time or 1600{degree}C with 2 s hold, conditions which give the maximum release of nitrogen from the char. 18 refs., 8 figs.

  19. Pulverized coal firing of aluminum melting furnaces. First annual technical progress report, May 1978-June 1979

    Energy Technology Data Exchange (ETDEWEB)

    West, C.E.; Hines, J.E.; Stewart, D.L. Jr.; Yu, H.

    1979-10-01

    The ultimate objective of this program is the commercial demonstration of an efficient, environmentally acceptable coal firing process suitable for implementation on melting furnaces throughout the aluminum industry. To achieve this goal, the program has been divided into two phases. Phase I has begun with the design and construction of a 350 lb/h (coal) staged slagging cyclone combustor (SSCC) attached to a 7-ft dia aluminum melting ladle furnace. Process development will culminate with a 1000 pph prototype SSCC firing a 40,000 lb capacity open hearth melting furnace at the Alcoa Laboratories. Phase II implementation is currently planned for Alcoa's Lafayette, IN, Works, where two of the ingot plant's five open hearth melting furnaces will be converted to utilize coal. In addition to confirmation of data gathered in Phase I, the effect of extended production schedule operation on equipment and efficiencies will be determined. This work would begin in 1982 pursuant to technical and economic evaluation of the process development at that time. A major design subcontract for assistance in the design of the SSCC is 80% completed.

  20. Assessment against Experiments of Devolatilization and Char Burnout Models for the Simulation of an Aerodynamically Staged Swirled Low-NOx Pulverized Coal Burner

    Directory of Open Access Journals (Sweden)

    Marco Torresi

    2017-01-01

    Full Text Available In the next few years, even though there will be a continuous growth of renewables and a loss of the share of fossil fuel, energy production will still be strongly dependent on fossil fuels. It is expected that coal will continue to play an important role as a primary energy source in the next few decades due to its lower cost and higher availability with respect to other fossil fuels. However, in order to improve the sustainability of energy production from fossil fuels, in terms of pollutant emissions and energy efficiency, the development of advanced investigation tools is crucial. In particular, computational fluid dynamics (CFD simulations are needed in order to support the design process of low emission burners. Even if in the literature several combustion models can be found, the assessment of their performance against detailed experimental measurements on full-scale pulverized coal burners is lacking. In this paper, the numerical simulation of a full-scale low-NO x , aerodynamically-staged, pulverized coal burner for electric utilities tested in the 48 MW th plant at the Combustion Environment Research Centre (CCA - Centro Combustione e Ambiente of Ansaldo Caldaie S.p.A. in Gioia del Colle (Italy is presented. In particular, this paper is focused on both devolatilization and char burnout models. The parameters of each model have been set according to the coal characteristics without any tuning based on the experimental data. Thanks to a detailed description of the complex geometry of the actual industrial burner and, in particular, of the pulverized coal inlet distribution (considering the entire primary air duct, in order to avoid any unrealistic assumption, a correct selection of both devolatilization and char burnout models and a selection of suited parameters for the NO x modeling, accurate results have been obtained in terms of NO x formation. Since the model parameters have been evaluated a priori, the numerical approach proposed

  1. Synergistic Utilization of Coal Fines and Municipal Solid Waste in Coal-Fired Boilers. Phase I Final Report

    Energy Technology Data Exchange (ETDEWEB)

    V. Zamansky; P. Maly; M. Klosky

    1998-06-12

    A feasibility study was performed on a novel concept: to synergistically utilize a blend of waste coal fines with so-called E-fuel for cofiring and reburning in utility and industrial boilers. The E-fuel is produced from MSW by the patented EnerTech's slurry carbonization process. The slurry carbonization technology economically converts MSW to a uniform, low-ash, low-sulfur, and essentially chlorine-free fuel with energy content of about 14,800 Btu/lb.

  2. HT-L与Shell及Texaco粉煤气化技术的比较%Technological Comparison of HT-L with Shell and Texaco Pulverized Coal Gasification Processes

    Institute of Scientific and Technical Information of China (English)

    吴胜军

    2011-01-01

    介绍了HT-L粉煤气化技术的工艺特点,并从比氧耗、有效气成分、煤气化效率、能耗等方面与Shell 及Texaco粉煤气化技术进行了分析比较.结果表明:HT-L粉煤气化技术具有高效节能、煤种适用范围广、气化效率高、能耗低、建设和运行成本低、工艺成熟可靠并具有自主知识产权的优点,具有广阔的发展前景.%Process features are described of the HT-L pulverized coal gasification technology, and an analytical comparison is done with the Shell and Texaco pulverized coal gasification technology in terms of specific oxygen consumption, active gas constituent, coal gasification efficiency, and energy consumption. The results show that the HT-L technology has the advantages of highly efficient energy saving, wide scope of application to various coal types, high gasification efficiency, low energy consumption, low construction and operation cost, mature and reliable technology, and possession of independent intellectual property, and so it brings about broad prospects for development.

  3. Numerical simulation of NOx formation in a cyclone-opposed coal-fired utility boiler

    Institute of Scientific and Technical Information of China (English)

    LI Fang-qin; REN Jian-xing; WEI Dun-song

    2005-01-01

    In this paper, FLUENT software was used to simulate the burning process in a utility boiler. Chose the kinetics/diffusion-limited as combustion model, two-compet-ingrates as devolatjlization model, RNG k-εmodel as viscous model, and PDF model as combustion turbulent flow model. Numerical calculation of NOx formation in a 330 MW cyclone-opposed coal-fired utility boiler with 32 double air registers was done. The distribution characteristics of temperature, NOx and oxygen concentration in furnace were studied. They were symmetrically distributed in furnace. In the combustion area, temperature and NOx concentration are high, while oxygen concentration is low. Temperature and NOx concentration are declined gradually along with furnace height, while oxygen concentration is raised. The higher the temperature is and the greater the excess air coefficient is, the more NOx formation.

  4. Selection of Special Valves in Pulverized Coal Gasiifcation Industry%粉煤气化特殊阀门选型

    Institute of Scientific and Technical Information of China (English)

    张赫

    2016-01-01

    China is a country of ‘lean oil, less gas, rich in coal’, therewith the technology of coal gasification is an important means to realize the clean and efficient use of coal. Moreover the technology of pressured pulverized coal gasification recognized as a mature technology in the industry possess advantages of large production capacity and high gasification efficiency. However, the erosion of special valve from abrasion by particles of process fluid can be serious, which will cause the short service cycle and huge economic losses. This paper is based on the successful experience in the similar domestic plants among these years, summarize the application of variety of special valves in the industry, put forward suggestions of instrument selection, and provide the reference for the engineering of similar projects in the future.%我国是一个“贫油、少气、富煤”的国家,煤气化技术是实现煤炭清洁高效利用的重要手段。粉煤加压气化技术是目前业内认可较为成熟的技术,具有生产能力大、气化效率高的特点。然而由于其工艺介质的特点,其中所应用的特殊阀门磨损严重,使用周期短,导致装置频繁停车,造成了巨大的经济损失。本文根据近些年国内粉煤气化的成功运行经验,对其中多种特殊应用的阀门使用进行了总结探讨,提出建议的仪表选型,为同类项目的仪表设计工作提供参考依据。

  5. 300 MW机组磨煤机总风门优化控制的应用研究%Research on the Application of Optimization Control in Total Air Damper of Coal Pulverizers in 300 MW Power Generation Unit

    Institute of Scientific and Technical Information of China (English)

    姜烈伟

    2013-01-01

    通过分析总风门控制回路及其执行机构的现场环境,找到了造成韶关电厂300 MW机组磨煤机总风门故障的原因.针对故障原因,提出了解决气缸内活塞在全开位置不固定的方案.该方案重新设计了控制原理图,完善了行程开关检测方式.实际运行证明,该方案能够满足机组负荷需求,保证了锅炉安全运行,达到了节能降耗的目的.%Through analyzing the site environment of the control loop and its actuator, the causes of the malfunctions of the total air damper of coal pulverizers in 300 MW power generating unit of Shaoguan power plant are found. In accordance with the causes of malfunctions, the strategy for solving the problem of unfixed fully open position of piston in air cylinder is proposed. The control principle of the strategy has been redesigned, the detection pattern of the travel switch is improved. The practical operation verifies that the correctness of the design scheme meets the load demand of the unit, ensures the safety operation of boiler, and reaches the goal of energy conservation.

  6. CONDENSING ECONOMIZERS FOR SMALL COAL-FIRED BOILERS AND FURNACES PROJECT REPORT - JANUARY 1994

    Energy Technology Data Exchange (ETDEWEB)

    BUTCHER,T.A.

    1994-01-04

    Condensing economizers increase the thermal efficiency of boilers by recovering sensible and latent heat from exhaust gas. These economizers are currently being used commercially for this purpose in a wide range of applications. Performance is dependent upon application-specific factors affecting the utility of recovered heat. With the addition of a condensing economizer boiler efficiency improvements up to 10% are possible. Condensing economizers can also capture flue gas particulates. In this work, the potential use of condensing economizers for both efficiency improvement and control of particulate emissions from small, coal water slurry-fired boilers was evaluated. Analysis was done to predict heat transfer and particulate capture by mechanisms including: inertial impaction, interception, diffusion, thermophoretic forces, and condensation growth. Shell-and-tube geometries were considered with flue gas on the outside of Teflon-covered tubes. Experimental studies were done with both air- and water-cooled economizers refit to a small boiler. Two experimental arrangements were used including oil-firing with injection of flyash upstream of the economizer and direct coal water slurry firing. Firing rates ranged from 27 to 82 kW (92,000 to 280,000 Btu/hr). Inertial impaction was found to be the most important particulate capture mechanism and removal efficiencies to 95% were achieved. With the addition of water sprays directly on the first row of tubes, removal efficiencies increased to 98%. Use of these sprays adversely affects heat recovery. Primary benefits of the sprays are seen to be the addition of small impaction sites and future design improvements are suggested in which such small impacts are permanently added to the highest velocity regions of the economizer. Predicted effects of these added impactors on particulate removal and pressure drop are presented.

  7. CFD modeling of ash deposition for co-combustion of MBM with coal in a tangentially fired utility boiler

    NARCIS (Netherlands)

    Taha, T.J.; Stam, A.F.; Stam, K.; Brem, G.

    2013-01-01

    Ash deposition is one of the main challenges that needs to be tackled in response to increased percentage of biomass co-firing in pulverized fuel boilers. In this study, a model has been developed to investigate the slagging behavior of meat and bone meal (MBM) at higher co-firing rates in the Maasv

  8. Characterization of bottom ashes from coal pulverized power plants to determine their potential use feasibility

    Energy Technology Data Exchange (ETDEWEB)

    Menendez, E.; Alvaro, A. M.; Argiz, C.; Parra, J. L.; Moragues, A.

    2013-07-01

    The disposal of coal by products represents environmental and economical problems around the world. Therefore, the reuse and valorisation of this waste has become an important issue in the last decades. While high-value construction products containing fly ash were developed and its use is actually totally accepted as an addition to cement, the use of the bottom ash as supplementary cementitious material has not been allow. This paper examines the chemical and physical properties of fly ashes and bottom ashes from two different coal power plants in order to compare them and analyse the potential feasibility of bottom ash as cement replacement. The mechanical properties of cement mortars made with different percentages of both ashes were also study. The results obtained showed similar chemical composition of both kinds of ashes. The compressive strength values of mortars with 10 % and 25 % of cement replacement (at 28 days) were above the limits established in European standards and there were not significant differences between fly ash and bottom ash from both origins. (Author)

  9. Combustion of pulverized coal in vortex structures. Final report, October 1, 1993--December 31, 1995

    Energy Technology Data Exchange (ETDEWEB)

    Gollahalli, S.R.; Butuk, N.

    1996-03-01

    The objectives of the project were: (i) to understand the effects of heating one of the streams on the characteristics of shear layers, (ii) to investigate the changes in the characteristics of large scale vortex structures in the shear layer caused by the introduction of inert solid particles in one of the feed streams; (iii) to understand the effects of pyrolyzing solids on the shear layer behavior; and (iv) to study the effects of combustion of particles and their pyrolysis products on the shear layer structure, heat release rate, and pollutant emission characteristics. An experimental facility for generating two-dimensional shear layers containing vortex structures has been designed and fabricated. The experimental facility is essentially a low speed wind tunnel designed to (i) provide two gas streams, initially with uniform velocity profiles and isotropic turbulence, mixing at the end of a splitter plate, (ii) introduce vorticity by passively perturbing one of the streams, (iii) allow heating of one of the streams to temperatures high enough to cause pyrolysis of coal particles, and (iv) provide a natural gas flame in one of the streams to result in ignition and burning of coal particles.

  10. Gaseous corrosion of alloys and novel coatings in simulated environments for coal, waste and biomass boilers

    Energy Technology Data Exchange (ETDEWEB)

    Kalivodova, J.; Baxter, D. [JRC Petten, Clean Energies Unit, Postbus 2, 1755 ZG Petten (Netherlands); Schuetze, M.; Rohr, V. [DECHEMA e.V. Theodor-Heuss-Allee 25, 60486 Frankfurt (Germany)

    2005-12-01

    The reduction of emissions from power generation plants is a key part of the Kyoto Protocol. Reduced emissions per unit of power produced can be achieved via increased thermal efficiency and this can be achieved by increasing steam parameters (i.e. temperature and pressure). Increased steam parameters in turn leads to accelerated corrosion of boiler components. Biomass and solid waste fuels introduce a number of aggressive species into process environments that result in enhanced rates of boiler degradation. This paper reports on studies, both theoretical and experimental, of the corrosion behaviour of high-alloy steels and Ni-base alloys as well as coatings for use in high efficiency coal and/or biomass- and waste-fired power plants. Coatings produced within the SUNASPO project have been laboratory tested in gaseous atmospheres representative of coal combustion, biomass combustion and waste incineration. Laboratory tests were carried out mainly in the temperature range 500 C to 800 C. Initial results showed the poor performance of traditional uncoated low-alloy boiler steels P91 (9% Cr) and HCM12A (12% Cr), as well as the higher alloy steel, 17Cr/13Ni. Results show the beneficial effects of coatings containing Al, Si, Al + Si, Al + Ti and Al + B in reducing the rate of corrosive attack. In a combustion product gas containing 100 ppm HCl and 1000 ppm SO{sub 2}, aluminizing affords corrosion resistance of low-alloy steels such as HCM12A and P91 similar to that of Alloy 800 over 1000 h of test. The presence of Al inhibits internal, sometimes localized corrosion by promoting the formation of a protective surface oxide layer even at relatively low temperatures. The results of experiments in simulated coal; biomass and waste atmospheres are presented and discussed in terms of both corrosion kinetics and mechanisms of degradation. (Abstract Copyright [2005], Wiley Periodicals, Inc.)

  11. Visualization of 3-D temperature distribution in a 300 MW twin-furnace coal-fired boiler

    Institute of Scientific and Technical Information of China (English)

    YANG Chao; ZHOU Huai-chun; HUANG Zhi-feng

    2008-01-01

    Until now, it has been difficult to obtain on-line three-dimensional (3-D) temperature distribution information which can reflect the overall combustion condition in the furnace of a coal-fired power plant boiler. A combustion monitoring system is intro-duced which can solve the problem efficiently. Through this system, the 3-D temperature distribution in a coal-fired boiler furnace can be obtained using a novel flame image processing technique. Briefly, we first outline the visualization principle. Then, the hardware and software design of the system in a 300 MW twin-furnace coal-fired boiler are introduced in detail. The visualization of the 3-D temperature distribution in the twin-furnace boiler is realized with an industrial computer and the Distributed Control System (DCS) of the boiler. The practical operation of the system shows that it can provide valuable combustion information of a furnace and is useful for the combustion diagnosis and adjustment in coal-fired power plants.

  12. Operation corrosion test of austenitic steel bends for supercritical coal boilers

    Directory of Open Access Journals (Sweden)

    Cizner J.

    2016-03-01

    Full Text Available Corrosion tests of both annealed and not annealed bends of HR3C and S304H steels in operation conditions of black and brown coal combustion boilers in EPRU and EDE. After a long-term exposure, the samples were assessed gravimetrically and metallographically. The comparison of annealed and unannealed states showed higher corrosion rates in the annealed state; corrosion of the sample surface did not essentially differ for compression and tensile parts of the beams. Detailed assessment of both steels is described in detail in this study.

  13. Co-firing of paper mill sludge and coal in an industrial circulating fluidized bed boiler.

    Science.gov (United States)

    Tsai, Meng-Yuan; Wu, Keng-Tung; Huang, Chin-Cheng; Lee, Hom-Ti

    2002-01-01

    Co-firing of coal and paper mill sludge was conducted in a 103 MWth circulating fluidized bed boiler to investigate the effect of the sludge feeding rate on emissions of SOx, NOx, and CO. The preliminary results show that emissions of SOx and Nx decrease with increasing sludge feeding rate, but CO shows the reverse tendency due to the decrease in combustion temperature caused by a large amount of moisture in the sludge. All emissions met the local environmental requirements. The combustion ashes could be recycled as feed materials in the cement manufacturing process.

  14. High-Temperature Behavior of a NiCr-Coated T91 Boiler Steel in the Platen Superheater of Coal-Fired Boiler

    Science.gov (United States)

    Chatha, Sukhpal Singh; Sidhu, Hazoor S.; Sidhu, Buta S.

    2013-06-01

    Ni-20Cr coating was deposited on T91 boiler tube steel by high-velocity oxy-fuel (HVOF) process to enhance high-temperature oxidation resistance. High-temperature performance of bare, as well as HVOF-coated steel specimens was evaluated for 1500 h under in the platen superheater zone of coal-fired boiler, where the temperature was around 900 °C. Experiments were carried out for 15 cycles, each of 100-h duration followed by 1-h cooling at ambient temperature. The extent of degradation of the specimens was assessed by the thickness loss and depth of internal corrosion attack. Ni-20Cr-coated steel performed better than the uncoated steel in actual boiler environment. The improved degradation resistance of Ni-20Cr coating can be attributed to the presence of Cr2O3 in the top oxide scale and dense microstructure.

  15. The effects of coal quality on NO{sub x} emissions and carbon burnout in pulverised coal-fired utility boilers

    Energy Technology Data Exchange (ETDEWEB)

    O`Connor, M. [National Power plc, Swindon (United Kingdom)

    1999-04-01

    A comprehensive study is reported on the impact of coal quality on nitrogen oxides emissions and carbon burnout in utility boilers, with the aim of assessing their relationship and developing predictive tools for assessing coals. Experimental work was carried out on various laboratory-scale apparatus and on single burner test facilities ranging from 160 kW{sub th} to 40 MW{sub th} in size and measurements were obtained from full-scale 500 MW{sub e} utility boiler trials. This data and basic coal data were then used to develop mathematical models to predict full-scale boiler performance with respect to NO{sub x} emissions and carbon burnout. Power station trials demonstrated that coal quality effects nitrogen oxides and burnout. The variability in boiler conditions also impacted on these factors. Lower nitrogen and higher volatile coals generally produced less NO{sub x}. Volatile content was the most important generic coal property for predicting burnout. Modelling rig tests, using data from advanced laboratory-scale tests, were found to be just as successful as using rig tests for predicting NO{sub x} performance of different coals. Laboratory-scale tests were found to be successful in providing accurate predictions of burnout for the coals studied. Mathematical models, however, were found to be less successful in this area and further work to develop this is required. A major achievement was CFD solutions of full-scale utility boiler furnaces in a single mesh. 32 refs., 15 figs., 33 tabs., 2 apps.

  16. The effect of char structure on burnout during pulverized coal combustion at pressure

    Energy Technology Data Exchange (ETDEWEB)

    Liu, G.; Wu, H.; Benfell, K.E.; Lucas, J.A.; Wall, T.F.

    1999-07-01

    An Australian bituminous coal sample was burnt in a drop tube furnace (DTF) at 1 atm and a pressurized drop tube furnace (PDTF) at 15 atm. The char samples were collected at different burnout levels, and a scanning electron microscope was used to examine the structures of chars. A model was developed to predict the burnout of char particles with different structures. The model accounts for combustion of the thin-walled structure of cenospheric char and its fragmentation during burnout. The effect of pressure on reaction rate was also considered in the model. As a result, approximately 40% and 70% cenospheric char particles were observed in the char samples collected after coal pyrolysis in the DTF and PDTF respectively. A large number of fine particles (< 30 mm) were observed in the 1 atm char samples at burnout levels between 30% and 50%, which suggests that significant fragmentation occurred during early combustion. Ash particle size distributions show that a large number of small ash particles formed during burnout at high pressure. The time needed for 70% char burnout at 15 atm is approximately 1.6 times that at 1 atm under the same temperature and gas environment conditions, which is attributed to the different pressures as well as char structures. The overall reaction rate for cenospheric char was predicted to be approximately 2 times that of the dense chars, which is consistent with previous experimental results. The predicted char burnout including char structures agrees reasonably well with the experimental measurements that were obtained at 1 atm and 15 atm pressures.

  17. Reactivities of Blair Athol and Nang Tong coals in relation to their behavior in PFBC boiler

    Energy Technology Data Exchange (ETDEWEB)

    Miftahul Huda; Yozo Korai; Isao Mochida [Kyushu University, Fukuoka (Japan). Institute of Material Chemistry and Engineering

    2004-11-01

    The combustion reactivities of Blair Athol (BA) and Nang Tong (NT) coals were measured by thermogravimetry to understand their different behaviors in the PFBC boiler. The reactivity of BA was much the same as that of NT coal but their chars showed different characteristics. BA char of higher surface area (25 m{sup 2}/g) showed slightly higher reactivity than that of NT char of smaller surface area (7 m{sup 2}/g). BA coal showed heterogeneous ignition even at its particle size of as large as +355 {mu}m while NT coal showed homogeneous ignition at the average particle size over 75 {mu}m heterogenous one occurring with finer particle size (-75 {mu}m). Higher calorific value of BA volatile matter and higher reactivity of its char than those of NT coal causes of its heterogeneous ignition with an intense DTA peak, which may lead to local heating at its combustion and to yield reactive CaO from limestones causing of bed materials agglomeration in the PFBC. 15 refs., 8 figs., 2 tabs.

  18. Update of progress for Phase II of B&W`s advanced coal-fired low-emission boiler system

    Energy Technology Data Exchange (ETDEWEB)

    McDonald, D.K. [Babcock & Wilcox, Barberton, OH (United States); Madden, D.A.; Rodgers, L.W. [Babcock & Wilcox, Alliance, OH (United States)] [and others

    1995-11-01

    Over the past five years, advances in emission control techniques at reduced costs and auxiliary power requirements coupled with significant improvements in steam turbine and cycle design have significantly altered the governing criteria by which advanced technologies have been compared. With these advances, it is clear that pulverized coal technology will continue to be competitive in both cost and performance with other advanced technologies such as Integrated Gasification Combined Cycle (IGCC) or first generation Pressurized Fluidized Bed Combustion (PFBC) technologies for at least the next decade. In the early 1990`s it appeared that if IGCC and PFBC could achieve costs comparable to conventional pulverized coal plants, their significantly reduced NO{sub x} and SO{sub 2} emissions would make them more attractive. A comparison of current emission control capabilities shows that all three technologies can already achieve similarly low emissions levels.

  19. Comparative analysis of the influence of turbulence models on the description of the nitrogen oxides formation during the combustion of swirling pulverized coal flow

    Science.gov (United States)

    Kuznetsov, V.; Chernetskaya, N.; Chernetskiy, M.

    2016-10-01

    The paper presents the results of numerical research on the influence of the two- parametric k-ε, and k-ω SST turbulence models as well as Reynolds stress model (RSM) on the description of the nitrogen oxides formation during the combustion of pulverized coal in swirling flow. For the numerical simulation of turbulent flow of an incompressible liquid, we used the Reynolds equation taking into account the interfacial interactions. To solve the equation of thermal radiation transfer, the P1 approximation of spherical harmonics method was employed. The optical properties of gases were described based on the sum of gray gases model. To describe the motion of coal particles we used the method of Lagrange multipliers. Burning of coke residue was considered based on diffusion - kinetic approximation. Comparative analysis has shown that the choice of turbulence model has a significant impact on the root mean square (RMS) values of the velocity and temperature pulsation components. This leads to significant differences in the calculation of the nitrogen oxides formation process during the combustion of pulverized coal.

  20. Comparison of pilot-scale furnace experiments and predictions to full-scale boiler performance of compliance coals

    Energy Technology Data Exchange (ETDEWEB)

    Monroe, L.S. [Southern Research Inst., Birmingham, AL (United States); Clarkson, R.J. [Southern Co. Services, Inc., Birmingham, AL (United States); Stallings, J.W. [Electric Power Research Inst., Palo Alto, CA (United States)

    1996-01-01

    A series of compliance coals have been fired in the Southern Company Services and Southern Research Institute pilot-scale Combustion Research Facility, with the goal of predicting NO{sub x} emissions, unburned carbon levels, and other operating parameters. The research was financed by a tailored collaboration between Alabama Power and the Electric Power Research Institute. The coals included a South American coal, a Powder River Basin coal, and several local Alabama bituminous coals. They were fired in conventional and low NO{sub x} firing modes, where some of the coals were fired in a tangential-fired simulation, others as wall-fired, and some in both types of firing. Two of Alabama Power`s boilers were used as the plants simulated in the pilot-scale experiments, along with a Gulf Power boiler. The results of the NO{sub x} emissions and unburned carbon from the pilot furnace testing are presented and compared to the limited full-scale boiler data available on these coals.

  1. Fundamental study of the pulverized coal char combustion in oxyfuel mode with drop tube furnace

    Energy Technology Data Exchange (ETDEWEB)

    Ito, Takamasa; Takafuji, Makoto; Suda, Toshiyuki; Fujimori, Toshiro [Heat and Fluid Dynamics Department, Yokohama (Japan)

    2013-07-01

    The combustion characteristics of coal char particles in either O{sub 2}/N{sub 2} or O{sub 2}/CO{sub 2} conditions were experimentally investigated. Especially, the char burnout, the char particle temperature and the shrinkage of the char particles were discussed. A Drop Tube Furnace (DTF: whose wall temperature was set at 873, 923 and 973 K) was used as the experimental apparatus. The experimental results revealed that, in equivalent oxygen concentration, the char burnout and the char particle temperature were higher in O{sub 2}/N{sub 2} conditions than those in O{sub 2}/CO{sub 2} conditions. The shrinkage of the char particle did not show the large difference in either O{sub 2}/N{sub 2} or O{sub 2}/CO{sub 2} conditions. Up to 15% of char burnout, the char particle diameters were reduced gradually. Up to 80% of char burnout, the char particle diameters were not changed. This is supposed that the chemical reaction is mainly occurred not on the external surface but on the internal surface of the char particle. Over 80% of char burnout, sudden shrinkage could be seen. Finally, an empirical equation for the prediction of the char particle shrinkage was introduced. Further investigation is required in high operating temperature, where CO{sub 2} gasification may have a large influence on the char burnout.

  2. The Mechanisms of Flame Stabilization and Low NOx Emission in an Eccentric Jet Pulverized Coal Combustor

    Institute of Scientific and Technical Information of China (English)

    SunWenchao; SunYezhu; 等

    1992-01-01

    The mechanisms of flame stabilization and low NOx emission features of an accentric jet pulverzed coal combustor were studied through numerical modelling and experimental investigation.The results show that the formation of the unique flowfield structure is closely related to the interaction among combustor configuration.the primary jet and the control Jet.and that certain rules should be follwed in orber to obtain the optimum condition for flame stabilization.The distributions of temperature and concentration of NO,O2,CO and CO2 inside the combustor were experimentally measured.The effects of strustural and operational parameters on combustion and NO formation were studied.It was found that reduction of primary air,suitable use of control jet and reasonable uptilt angle of the primary jet all contributed to the reduction of NOx at the combustor exit.A new hypothesis,that reasonable separation of oxygen and fuel within the fuel-rich zone is beneficial to further reduction of NOx emission,is given,The study showed that good compatibility existed between the capability of flame stabilization and low NOX emission for this type of combustor.

  3. FUNDAMENTAL INVESTIGATION OF FUEL TRANSFORMATIONS IN PULVERIZED COAL COMBUSTION AND GASIFICATION TECHNOLOGIES

    Energy Technology Data Exchange (ETDEWEB)

    Robert Hurt; Joseph Calo; Thomas H. Fletcher; Alan Sayre

    2005-04-29

    The goal of this project was to carry out the necessary experiments and analyses to extend current capabilities for modeling fuel transformations to the new conditions anticipated in next-generation coal-based, fuel-flexible combustion and gasification processes. This multi-organization, multi-investigator project has produced data, correlations, and submodels that extend present capabilities in pressure, temperature, and fuel type. The combined experimental and theoretical/computational results are documented in detail in Chapters 1-8 of this report, with Chapter 9 serving as a brief summary of the main conclusions. Chapters 1-3 deal with the effect of elevated pressure on devolatilization, char formation, and char properties. Chapters 4 and 5 deal with advanced combustion kinetic models needed to cover the extended ranges of pressure and temperature expected in next-generation furnaces. Chapter 6 deals with the extension of kinetic data to a variety of alternative solid fuels. Chapter 7 focuses on the kinetics of gasification (rather than combustion) at elevated pressure. Finally, Chapter 8 describes the integration, testing, and use of new fuel transformation submodels into a comprehensive CFD framework. Overall, the effects of elevated pressure, temperature, heating rate, and alternative fuel use are all complex and much more work could be further undertaken in this area. Nevertheless, the current project with its new data, correlations, and computer models provides a much improved basis for model-based design of next generation systems operating under these new conditions.

  4. Qualitative analysis of coal combusted in boilers of the thermal power plants in Bosnia and Herzegovina

    Directory of Open Access Journals (Sweden)

    Đurić Slavko N.

    2012-01-01

    Full Text Available In this paper we have looked into the qualitative analysis of coals in Bosnia and Herzegovina (B-H. The analysis includes the following characteristics: moisture (W, ash (A, combustible matter (Vg and lower heating value (Hd. From the statistic parameters we have determined: absolute range (R, arithmetic mean (X, standard deviation (S and variations coefficient (Cv. It has been shown that the coal characteristics (W, A, Vg, Hd have normal distribution. The analysis show that there are considerable deviations of ash characteristics: moisture (36.23%, ash (34.21%, combustible matter (16.15% and lower heating value (25.16% from the mean value which is shown by the variations coefficient (Cv. Large oscilations of mass portions: W, A, Vg and Hd around the mean value can adversely influence the function of a boiler plant and an electric filter plant in thermal power plants in B-H in which the mentioned types of coal burn. Large ash oscilations (34.21% around the mean value point out to the inability of application of dry procedures of desulphurisation of smoke gasses (FGD due to the additional quantity of ash. It has been shown that the characteristics of Bosnian types of coal do not deviate a lot from the characteristics of coal in the surrounding countries (coals of Serbia and Monte Negro. The results can be used in analysis of coal combustion in thermal power plants, optimisation of electrical-filtre, reduction of SO2 in smoke gas and other practical problems.

  5. Analytical model for erosion behaviour of impacted fly-ash particles on coal-fired boiler components

    Indian Academy of Sciences (India)

    S K Das; K M Godiwalla; S P Mehrotra; K K M Sastry; P K Dey

    2006-10-01

    Fly ash particles entrained in the flue gas from boiler furnaces in coal-fired power stations can cause serious erosive wear on steel surfaces along the flow path. Such erosion can significantly reduce the operational life of the boiler components. A mathematical model embodying the mechanisms of erosion on behaviour, has been developed to predict erosion rates of coal-fired boiler components at different temperatures. Various grades of steels used in fabrication of boiler components and published data pertaining to boiler fly ash have been used for the modelling. The model incorporates high temperature tensile properties of the target metal surface at room and elevated temperatures and has been implemented in an user-interactive in-house computer code (EROSIM–1), to predict the erosion rates of various grades of steel. Predictions have been found to be in good agreement with the published data. The model is calibrated with plant and experimental data generated from a high temperature air-jet erosion-testing facility. It is hoped that the calibrated model will be useful for erosion analysis of boiler components.

  6. Analytical model for erosion behaviour of impacted fly-ash particles on coal-fired boiler components

    Energy Technology Data Exchange (ETDEWEB)

    Das, S.K.; Godiwalla, K.M.; Mehrotra, S.P.; Sastry, K.K.M.; Dey, P.K.

    2006-10-15

    Fly ash particles entrained in the flue gas from boiler furnaces in coal-fired power stations can cause serious erosive wear on steel surfaces along the flow path. Such erosion can significantly reduce the operational life of the boiler components. A mathematical model, embodying the mechanisms of erosion on behaviour, has been developed to predict erosion rates of coal-fired boiler components at different temperatures. Various grades of steels used in fabrication of boiler components and published data pertaining to boiler fly ash have been used for the modelling. The model incorporates high temperature tensile properties of the target metal surface at room and elevated temperatures and has been implemented in an user-interactive in-house computer code (EROSIM-1), to predict the erosion rates of various grades of steel. Predictions have been found to be in good agreement with the published data. The model is calibrated with plant and experimental data generated from a high temperature air-jet erosion-testing facility. It is hoped that the calibrated model will be useful for erosion analysis of boiler components.

  7. Co-firing of coal and paper mill sludge in a 103 MWth CFB boiler

    Energy Technology Data Exchange (ETDEWEB)

    Wu, K.T.; Lee, H.T. [Industrial Technology Research Inst., Hsinchu, (China). Energy and Resources Laboratories; Tsai, M.Y.; Huang, C.C. [Hsin Wu Mill, Yuen Foong Yu Paper Mfg. Co. Ltd., Taoyuan, (China)

    2002-07-01

    One of the advantages of circulating fluidized bed coal combustion technology is the ability to use a wide range of fuels with low atmospheric emissions. Co-firing coal with other solid wastes such as sludge, municipal waste systems (MWS) and biomass has been recently considered as an environmentally and economically sound method to produce energy while managing wastes. In this study, paper mill sludge from the Hsin Wu Mill in Taiwan was co-fired with coal in a 103 MW circulating fluidized bed boiler. The effect of the sludge feeding rate on emissions of SO{sub x}, NO{sub x} and CO was examined. The circulating fluidized bed was originally designed for burning coal only. Preliminary results indicate that emissions of SO{sub x} and NO{sub x} decrease with increasing sludge feeding rate. However, the reverse is true for CO emissions because of the decrease in combustion temperature resulting from a high moisture content in the sludge. All emissions met Taiwanese environmental standards. The study also showed that combustion ash can be recycled as a raw material for cement production. 7 refs., 4 tabs., 4 figs.

  8. Mercury reduction by coal blending : effects of boiler configuration and blending on mercury speciation

    Energy Technology Data Exchange (ETDEWEB)

    Lyng, R. [Ontario Power Generation Nanticoke Generating Station, Nanticoke, ON (Canada)

    2006-07-01

    Ontario Power Generation has explored the potential of reducing mercury emissions through fuel blending on full-scale operating units at its 8 x 500 MW Nanticoke coal-fired generating station. This presentation addressed the issue of unit configuration on mercury speciation. It outlined full scale testing of mercury emissions in 2004 and the potential for mercury control suggested by the test data. Mercury emissions were measured for the firing of various eastern US bituminous and western US sub-bituminous Powder River Basin (PRB) coal blends. Three blends of up to 84 per cent sub-bituminous coal were tested. Two methods of coal blending, selective bunkering and silo or field blending were also tested. Mercury emissions under boiler configurations with and without selective catalytic reduction (SCR) and over-fire air were compared. This paper included the results from semi-continuous monitoring (SCM) data collected during the test period. A high mercury oxidation was observed over chlorine concentration ranges of 0.3 to 0.1 per cent. It was noted that feeding dedicated fuels to mills, rather than yard blends of bituminous PRB, results in higher levels of mercury capture, particularly at higher than 16:84 blend. A consistently high level of oxidation was noted across the SCR demonstrated for all blends tested. It was noted that Over Fire Air (OFA) advanced combustion technology systems appeared to increase mercury oxidation. tabs., figs.

  9. FUNDAMENTAL INVESTIGATION OF FUEL TRANSFORMATIONS IN PULVERIZED COAL COMBUSTION AND GASIFICATION TECHNOLOGIES

    Energy Technology Data Exchange (ETDEWEB)

    Robert Hurt; Joseph Calo; Thomas Fletcher; Alan Sayre

    2003-01-01

    The goal of this project is to carry out the necessary experiments and analyses to extend leading submodels of coal transformations to the new conditions anticipated in next-generation energy technologies. During the first project quarter, a technical kick-off meeting was held on the Brown campus involving PIs from Brown (Hurt, Calo), BYU (Fletcher), and B&W (Sayre, Burge). Following this first meeting the current version of CBK (Version 8) was transferred to B&W McDermott and the HP-CBK code developed by BYU was transferred to Brown to help guide the code development in this project. Also during the first project year, progress was reviewed at an all-hands meeting was held at Brigham Young University in August, 2001. The meeting was attended by PIs Fletcher, Hurt, Calo, and Sayre, and also by affiliated investigators Steven Burge from McDermott and Prof. William Hecker from BYU. During the first project year, significant progress was made on several fronts, as described in detail in the previous annual report. In the current second annual report, we report on progress made on two important project tasks. At Brown University: (1) Char combustion reactivities at 500 C in air were determined for a diverse set of solid fuels and organic model compound chars. These varied over 4 orders of magnitude for the chars prepared at 700 C, and over 3 orders of magnitude for the chars prepared at 1000 C. The resultant reactivities correlate poorly with organic elemental composition and with char surface area. (2) Specially-acquired model materials with minute amounts of inorganic matter exhibit low reactivities that fall in a narrow band as a function of wt-% carbon. Reactivities in this sample subset correlate reasonably well with total char surface area. (3) A hybrid chemical/statistical model was developed which explains most of the observed reactivity variation based on four variables: the amounts of nano-dispersed K, nanodispersed (Ca+Mg), elemental carbon (wt-% daf), and

  10. Development of Erosion-Corrosion-Resistant Cold-Spray Nanostructured Ni-20Cr Coating for Coal-Fired Boiler Applications

    Science.gov (United States)

    Kumar, M.; Singh, H.; Singh, N.; Chavan, N. M.; Kumar, S.; Joshi, S. V.

    2015-12-01

    The erosion-corrosion (E-C) behavior of a cold-spray nanostructured Ni-20Cr coating was studied under cyclic conditions in a coal-fired boiler. This study was done for 15 cycles (1500 h), in which each cycle comprised 100 h of heating in the boiler environment, followed by 1 h of cooling under ambient air conditions. The E-C extent was evaluated in terms of thickness loss data of the samples. The eroded-corroded samples were characterized using XRD, SEM/EDS, and x-ray mapping analyses. The nanostructured coating offered excellent E-C protection to boiler tube material (SA 516 steel) under harsh live conditions of the boiler. This E-C resistance offered by investigated coating may be attributed to the presence of protective NiO and Cr2O3 phases in its oxide scale and its superior as-sprayed microhardness.

  11. Development and testing of a high efficiency advanced coal combustor: Phase 3 industrial boiler retrofit. Final report

    Energy Technology Data Exchange (ETDEWEB)

    Patel, R.L.; Thornock, D.E.; Miller, B.G.; Scaroni, A.W.; McGowan, J.G.

    1998-03-01

    Economics and/or political intervention may one day dictate the conversion from oil or natural gas to coal in boilers that were originally designed to burn oil or gas. In recognition of this future possibility the US Department of Energy, Federal Energy Technical Center (DOE-FETC) supported a program led by ABB Power Plant Laboratories with support from the Energy and Fuels Research Center of Penn State University with the goal of demonstrating the technical and economic feasibility of retrofitting a gas/oil designed boiler to burn micronized coal. In support of the overall goal the following specific objectives were targeted: develop a coal handling/preparation system that can meet the technical and operational requirements for retrofitting microfine coal on a boiler designed for burning oil or natural gas; maintain boiler thermal performance in accordance with specifications when burning oil or natural gas; maintain NOx emissions at or below 0.6 lb NO{sub 2} per million Btu; achieve combustion efficiencies of 98% or higher; and determine economic payback periods as a function of key variables.

  12. 锅炉给粉变频调速系统%Varying Frequency Speed Adjustment System for Boiler Feeding Coal

    Institute of Scientific and Technical Information of China (English)

    张焕武

    2000-01-01

    This paper briefly introduces the design of varying frequency speed adjustment system for boiler feeding coal and simply introduces it's advantages.%简要介绍了锅炉给粉变频调速系统的设计,并概述了其优越性。

  13. DEVELOPMENT OF A NOVEL RADIATIVELY/CONDUCTIVELY STABILIZED BURNER FOR SIGNIFICANT REDUCTION OF NOx EMISSIONS AND FOR ADVANCING THE MODELING AND UNDERSTANDING OF PULVERIZED COAL COMBUSTION AND EMISSIONS

    Energy Technology Data Exchange (ETDEWEB)

    Noam Lior; Stuart W. Churchill

    2003-10-01

    The primary objective of the proposed study was the study and analysis of, and design recommendations for, a novel radiatively-conductively stabilized combustion (RCSC) process for pulverized coal, which, based on our prior studies with both fluid fuels and pulverized coal, holds a high promise to reduce NO{sub x} production significantly. We have primarily engaged in continuing and improving our process modeling and analysis, obtained a large amount of quantitative information about the effects of the major parameters on NO{sub x} production, conducted an extensive exergy analysis of the process, evaluated the practicalities of employing the Radiatively-Conductively Stabilized Combustor (RCSC) to large power and heat plants, and improved the experimental facility. Prior experimental work has proven the feasibility of the combustor, but slagging during coal combustion was observed and should be dealt with. The primary outcomes and conclusions from the study are: (1) we developed a model and computer program that represents the pulverized coal combustion in the RCSC, (2) the model predicts that NO{sub x} emissions can be reduced by a number of methods, detailed in the report. (3) the exergy analysis points out at least a couple of possible ways to improve the exergetic efficiency in this combustor: increasing the effectiveness of thermal feedback, and adjusting the combustor mixture exit location, (4) because of the low coal flow rates necessitated in this study to obtain complete combustion in the burner, the size of a burner operating under the considered conditions would have to be up to an order of magnitude, larger than comparable commercial burners, but different flow configurations of the RCSC can yield higher feed rates and smaller dimensions, and should be investigated. Related to this contract, eleven papers were published in journals and conference proceedings, and ten invited presentations were given at university and research institutions, as well as at

  14. Oxy-coal Combustion Studies

    Energy Technology Data Exchange (ETDEWEB)

    Wendt, J. [Univ. of Utah, Salt Lake City, UT (United States); Eddings, E. [Univ. of Utah, Salt Lake City, UT (United States); Lighty, J. [Univ. of Utah, Salt Lake City, UT (United States); Ring, T. [Univ. of Utah, Salt Lake City, UT (United States); Smith, P. [Univ. of Utah, Salt Lake City, UT (United States); Thornock, J. [Univ. of Utah, Salt Lake City, UT (United States); Y Jia, W. Morris [Univ. of Utah, Salt Lake City, UT (United States); Pedel, J. [Univ. of Utah, Salt Lake City, UT (United States); Rezeai, D. [Univ. of Utah, Salt Lake City, UT (United States); Wang, L. [Univ. of Utah, Salt Lake City, UT (United States); Zhang, J. [Univ. of Utah, Salt Lake City, UT (United States); Kelly, K. [Univ. of Utah, Salt Lake City, UT (United States)

    2012-01-06

    The objective of this project is to move toward the development of a predictive capability with quantified uncertainty bounds for pilot-scale, single-burner, oxy-coal operation. This validation research brings together multi-scale experimental measurements and computer simulations. The combination of simulation development and validation experiments is designed to lead to predictive tools for the performance of existing air fired pulverized coal boilers that have been retrofitted to various oxy-firing configurations. In addition, this report also describes novel research results related to oxy-combustion in circulating fluidized beds. For pulverized coal combustion configurations, particular attention is focused on the effect of oxy-firing on ignition and coal-flame stability, and on the subsequent partitioning mechanisms of the ash aerosol.

  15. Utilization of coal ash from fluidized-bed combustion boilers as road base material; Sekitandaki ryudoso boiler kara no sekitanbai no robanzai to shite no riyo

    Energy Technology Data Exchange (ETDEWEB)

    Shibata, Y. [Kawasaki Heavy Industries, Ltd., Kobe (Japan); Kozasa, K. [Center for Coal Utilization, Japan, Tokyo (Japan); Tsuzura, K. [Naruto Salt Mfg. Co. Ltd., Tokushima (Japan); Izumi, H. [Nippon Hodo Co. Ltd., Tokyo (Japan)

    1998-03-01

    Coal ash from the fluidized bed boiler is evaluated for its properties as is, as solidified or granulated, and as the roadbed material. The coal ash tested in the experiment is a mixture of ash from the fluidized bed boiler bottom, ash from the cyclone separator, and ash from the bag filter. In the manufacture of solid or granulated bodies, coal ashes are kneaded in water whose amount puts the mixture near the plasticization limit, are pressed in a low-pressure press and made into solid bodies by a 15-hour curing in 60degC saturated steam, and the solid bodies are crushed into solid granules. A content release test is conducted about the release of dangerous substances, and road paving experiments are conducted to learn the workability and serviceability of the granulated material as a road paving material. A study of the experimental results discloses what is mentioned below. Coal ash containing 10-20vol% of CaO and 15vol% or less of unburnt carbon turns into a high-strength solid after curing in saturated steam whose temperature is not higher than 60degC. The granulated solid satisfies the standards that an upper subbase material is expected to satisfy. It also meets the environmental standards in a release content test for soil set forth by Environment Agency notification No.46. 8 refs., 8 figs., 4 tabs.

  16. [An investigation of the formation of] polycyclic aromatic hydrocarbon (PAH) emissions when firing pulverized coal in a bench-scale drop tube reactor

    Energy Technology Data Exchange (ETDEWEB)

    Pisupati, S.V.; Wasco, R.S.; Scaroni, A.W. [Pennsylvania State Univ., University Park, PA (United States). Combustion Lab.

    1998-12-31

    The Clean Air Act Amendments (CAAA) of 1990 contain provisions which will set standards for the allowable emissions of 188 analytes designated as hazardous air pollutants (HAPs). This list of HAPs was used to establish an initial list of source categories for which EPA would be required to establish technology-based emission standards, which would result in regulated sources sharply reducing routine emissions of toxic air pollutants. Polycyclic organic matter (POM) has also been referred to as polynuclear or polycyclic aromatic compounds (PACs). Nine major categories of POM have been defined by EPA. The study of organic compounds from coal combustion is complex and the results obtained so far are inconclusive with respect to emission factors. The most common organic compounds in the flue gas of coal-fired power plants are polycyclic aromatic hydrocarbons (PAHs). Furthermore, EPA has specified 16 PAH compounds as priority pollutants. These are naphthalene, acenaphthylene, acenaphthene, fluorene, phenanthrene, anthracene, fluoranthene, pyrene, chrysene, benz[a]anthracene, benzo[b]fluoranthene, benzo[k]fluoranthene, benzo[a]pyrene, indeno[1,2,3-cd]pyrene, benzo[ghi]perylene, and dibenz[ah]anthracene. Penn State`s Combustion Laboratory is equipped to collect and analyze the HAPs in the flue gas from fossil fuels combustion. The overall objective of this study was to examine the effect of unit temperature on PAH emissions. A Modified Method 5 sampling train was used to isokinetically collect samples at desired locations in flue gas streams. The collected sample can be separated into solid, condensed liquid and gaseous phases. The PAHs of interest are extracted from the collected sample, concentrated, then separated and quantified by gas chromatography/mass spectrometry (GC/MS). This study was conducted using a bench-scale drop-tube reactor (DTR). The fuel selected for this study was a Middle Kittanning seam coal pulverized to 80% passing US Standard 200 mesh (commonly

  17. A comparison between ceramic membrane filters and conventional fabric filters for fine particulate removal from a coal-fired industrial boiler

    Energy Technology Data Exchange (ETDEWEB)

    Miller, B.G.; Wincek, R.T.; Glick, D.C.; Scaroni, A.W. [Pennsylvania State Univ., University Park, PA (United States); Drury, K. [Corning Inc., Painted Post, NY (United States); Makris [Corning Inc., Acton, MA (United States); Stubblefield, D.J. [Corning Inc., Corning, NY (United States)

    1998-12-31

    Penn State is developing technologies for ultralow emissions when firing coal-based fuels, i.e., micronized coal and coal-water slurry fuel (CWSF) in industrial boilers. Emissions being addressed are SO{sub 2}, NOx, fine particulate matter (PM{sub 10} and PM{sub 2.5}), and air toxics (trace elements and volatile organic compounds). Results from trace element and polynuclear aromatic hydrocarbon emissions testing, when firing coal-based fuels, are reported elsewhere in these proceedings. This paper discusses the evaluation of ceramic membrane filters for fine particulate removal in a package boiler when firing micronized coal and CWSF.

  18. Ash transformation in suspension fired boilers co-firing coal and straw

    DEFF Research Database (Denmark)

    Zheng, Yuanjing; Jensen, Peter Arendt; Jensen, Anker Degn

    To study the influence of local conditions on the reaction between gaseous KCl and kaolin or coal fly ash experiments were done on CHECs electrically heated entrained flow reactor, which can simulate the local conditions in suspension fired boilers. The experimental results were compared with model...... studied. Due to not completely well controlled conditions during the experiments only preliminary conclusions can be provided. For experiments done at 1100°C with a molar ratio of K/Si=0.3 and a residence time of 1.07s approximately 80% of potassium from KCl reacted with kaolin. A changed temperature...... (1100-1300 °C) or a changed amount of KCl (K/Si = 0.1 – 0.34) did only change the KCl conversion slightly. Si and Al rich coal ash seems to be less efficient to react with KCl compared to kaolin. However the applied coal ash had a larger particle size (d50 = 22μm) compared to the kaolin (d50 = 10μm)....

  19. 邯钢高炉喷吹煤粉的快速热解机制%Flash Pyrolysis of Pulverized Injection Coal at Hansteel

    Institute of Scientific and Technical Information of China (English)

    刘然; 高永亮; 王杏娟; 吕庆; 杜林森; 王竹民

    2012-01-01

    Aimed at increasing pulverized coal injection at Handan Steel,the pyrolysis of coal in raceway was simulated.The coal of CL and DW were selected and the decomposition rate was calculated by plasma pyrolysis.Gas products were analyzed by gas chromatography and morphology of residues were observed by scanning electron microscopy(SEM).The results show that CL and DW decomposition rate is 43.10% and 52.04% respectively and gas products of coal after plasma pyrolysis,which are different from general pyrolysis,consist of CO,H2,CH4,C2H2 and small content of C2H4,etc.Pyrolysis product has changed evidently,particle size become smaller.The vesicular structure occurs in coal grains when DW is added in the sample,which makes the specific surface area of coal grain increase.The solid carbon combustion ratio in tuyeres can be enhanced,which will provide the theoretical basis for pulverized coal combustion rate.%为了提高邯钢高炉喷吹煤比,模拟煤粉在高炉内的热解。以邯钢喷吹用长治煤(以下简称CL)和大湾煤(以下简称DW)为原料,采用等离子体进行快速热解,计算反应后煤粉的分解率,利用气相色谱仪对气体产物进行分析以及用扫描电镜(SEM)观察反应产物的形貌特征。试验结果表明,CL和DW的分解率分别为43.10%和52.04%,气相产物主要为CO、H2、CH4、C2H2及少量C2H4等气体,热解产物的粒径减小,形貌发生明显变化。在CL煤的基础上配加不同比例的DW后,煤粉颗粒出现了孔状结构,因此可以提高炉内风口回旋区固定碳颗粒的燃烧率,为提高煤粉燃烧率提供理论依据。

  20. Deposit formation in a full-scale pulverized wood-fired power plant with and without coal fly ash addition

    DEFF Research Database (Denmark)

    Wu, Hao; Shafique Bashir, Muhammad; Jensen, Peter Arendt

    2013-01-01

    temperatures of ~1300oC and ~800oC, respectively. It was found that during pulverized wood combustion, the deposit formation at the hightemperature location was characterized by a slow and continuous growth of deposits followed by the shedding of a large layer of deposits, while the deposit formation...

  1. Combining support vector regression and ant colony optimization to reduce NOx emissions in coal-fired utility boilers

    Energy Technology Data Exchange (ETDEWEB)

    Ligang Zheng; Hao Zhou; Chunlin Wang; Kefa Cen [Zhejiang University, Hangzhou (China). State Key Laboratory of Clean Energy Utilization

    2008-03-15

    Combustion optimization has recently demonstrated its potential to reduce NOx emissions in high capacity coal-fired utility boilers. In the present study, support vector regression (SVR), as well as artificial neural networks (ANN), was proposed to model the relationship between NOx emissions and operating parameters of a 300 MW coal-fired utility boiler. The predicted NOx emissions from the SVR model, by comparing with that of the ANN-based model, showed better agreement with the values obtained in the experimental tests on this boiler operated at different loads and various other operating parameters. The mean modeling error and the correlation factor were 1.58% and 0.94, respectively. Then, the combination of the SVR model with ant colony optimization (ACO) to reduce NOx emissions was presented in detail. The experimental results showed that the proposed approach can effectively reduce NOx emissions from the coal-fired utility boiler by about 18.69% (65 ppm). A time period of less than 6 min was required for NOx emissions modeling, and 2 min was required for a run of optimization under a PC system. The computing times are suitable for the online application of the proposed method to actual power plants. 37 refs., 8 figs., 3 tabs.

  2. NO{sub x} CONTROL OPTIONS AND INTEGRATION FOR US COAL FIRED BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    Mike Bockelie; Temi Linjewile; Connie Senior; Eric Eddings; Larry Baxter

    2003-04-29

    This is the eleventh Quarterly Technical Report for DOE Cooperative Agreement No: DE-FC26-00NT40753. The goal of the project is to develop cost effective analysis tools and techniques for demonstrating and evaluating low NO{sub x} control strategies and their possible impact on boiler performance for boilers firing US coals. The Electric Power Research Institute (EPRI) is providing co-funding for this program. This program contains multiple tasks and good progress is being made on all fronts. During this quarter, FTIR experiments for SCR catalyst sulfation were finished at BYU and indicated no vanadium/vanadyl sulfate formation at reactor conditions. Poisoned catalysts were prepared and tested in the CCS. Poisoning with sodium produced a noticeable drop in activity, which was larger at higher space velocity. A computer code was written at BYU to predict conversion along a cylindrical monolithic reactor. This code may be useful for monolith samples that will be tested in the laboratory. Shakedown of the slipstream reactor was completed at AEP's Rockport plant. Ammonia was connected to the reactor. The measurement of O{sub 2} and NO{sub x} made by the CEMs corresponded to values measured by the plant at the economizer outlet. Excellent NO{sub x} reduction was observed in preliminary tests of the reactor. Some operational problems were noted and these will be addressed next quarter.

  3. Application of the NOx Reaction Model for Development of Low-NOx Combustion Technology for Pulverized Coals by Using the Gas Phase Stoichiometric Ratio Index

    Directory of Open Access Journals (Sweden)

    Kenji Yamamoto

    2011-03-01

    Full Text Available We previously proposed the gas phase stoichiometric ratio (SRgas as an index to evaluate NOx concentration in fuel-rich flames. The SRgas index was defined as the amount of fuel required for stoichiometric combustion/amount of gasified fuel, where the amount of gasified fuel was the amount of fuel which had been released to the gas phase by pyrolysis, oxidation and gasification reactions. In the present study we found that SRgas was a good index to consider the gas phase reaction mechanism in fuel-rich pulverized coal flames. When SRgas < 1.0, NOx concentration was strongly influenced by the SRgas value. NOx concentration was also calculated by using a reaction model. The model was verified for various coals, particle diameters, reaction times, and initial oxygen concentrations. The most important reactions were gas phase NOx reduction reactions by hydrocarbons. The hydrocarbon concentration was estimated based on SRgas. We also investigated the ratio as an index to develop a new low-NOx combustion technology for pulverized coals. We examined the relation between local SRgas distribution in the fuel-rich region in the low-NOx flame and NOx emissions at the furnace exit, by varying burner structures. The relationship between local SRgas value and local NOx concentration was also examined. When a low-NOx type burner was used, the value of SRgas in the flame was readily decreased. When the local SRgas value was the same, it was difficult to influence the local NOx concentration by changing the burner structure. For staged combustion, the most important item was to design the burner structure and arrangement so that SRgas could be lowered as much as possible just before mixing with staged air.

  4. CFD simulation and experimental validation of co-combustion of chicken litter and MBM with pulverized coal in a flow reactor

    Energy Technology Data Exchange (ETDEWEB)

    Heikkinen, J.M.; Venneker, B.C.H.; di Nola, G.; de Jong, W.; Spliethoff, H. [Energy Technology section, Delft University of Technology, Leeghwaterstraat 44, NL-2628 CA Delft (Netherlands)

    2008-09-15

    The influence of co-combustion of solid biomass fuels with pulverized coal on burnout and CO emissions was studied using a flow reactor. The thermal input on a fuel feeding basis of the test rig was approximately 7 kW. Accompanied with the measurements, a reactor model using the CFD code AIOLOS was set up and first applied for two pure coal flames (with and without air staging). Reasonable agreement between measurements and simulations was found. An exception was the prediction of the CO concentration under sub-stoichiometric conditions (primary zone). As model input for the volatile matter release, the HTVM (high temperature volatile matter as defined by IFRF [IFRF, www.handbook.ifrf.net/handbook/glossary.html. ]) was used. Furthermore, a relatively slow CO oxidation rate obtained from the literature and the ERE (Extended Resistance Equation) model for char combustion were selected. Furthermore, the model was used for simulating co-firing of coal with chicken litter (CL) and meat and bone meal (MBM). The conditions applied are relevant for future co-firing practice with high thermal shares of secondary fuels (larger than 20%). The major flue gas concentrations were quite well described, however, CO emission predictions were only qualitatively following the measured trends when O{sub 2} is available and severely under-predicted under substoichiometric conditions. However, on an engineering level of accuracy, and concerning burnout, this work shows that co-combustion of the fuels can reasonably well be described with coal combustion sub-models. (author)

  5. Co-firing of Coal with Biomass and Waste in Full-scale Suspension-fired Boilers

    DEFF Research Database (Denmark)

    Dam-Johansen, Kim; Jappe Frandsen, Flemming; Jensen, Peter Arendt

    2013-01-01

    The energy policy in Denmark has for many years focused on lowering the net CO2 emission from heat and power production by replacing fossil fuels by renewable resources. This has been done by developing dedicated grate-fired boilers for biomass and waste fuels but also by developing coal......-based suspension-fired boilers to accept still higher fractions of biomass or waste material as fuels. This last development has been challenging of many reasons, including pre-treatment of fuels, and solving potential emission and operational problems during the simultaneous development of supercritical steam...

  6. Probabilistic approach to determining the optimum replacement of a superheater stage in 680 MW coal-fired boiler

    Energy Technology Data Exchange (ETDEWEB)

    Bos, Robert; Star, Ruud van der [Nuon Power Generation, Amsterdam (Netherlands)

    2009-07-01

    The boiler of the NUON power plant HW08 that went into operation in 1993 is designed as Benson boiler and mainly fired with hard coal. A creep-related tube failure occurred in the tertiary superheater that had been due to increased wall temperature caused by steam side formation of oxide layers. The theoretical lifetime of the components was calculated with the aid of the results of steam side oxide measurements and condition evaluation of the tertiary superheater with the aid of tube samples. The objective is to establish an operation and maintenance schedule for the desired operating lifetime of 300,000 hours. (orig.)

  7. Utilization of coal ash from fluidized-bed combustion boilers as road base material. Ryudosho boiler sekitan nenshobai no robanzai eno riyo

    Energy Technology Data Exchange (ETDEWEB)

    Ito, H.; Shibata, Y.; Takada, T.; Yamamuro, H. (Kawasaki Heavy Industries, Ltd., Tokyo (Japan))

    1994-07-20

    The present report reports the technological development to utilize coal ash from the fluidized-bed combustion boiler as a road base material. In case of mass production by low pressure press forming, the following hardening conditions are reported to be appropriate for kneading the ash only with water, curing it with steam and obtaining the higher compressive strength of thus hardened ash than 150kgf/cm[sup 2]: the boiler operational condition is to be adjusted so that the CaO content and char content may exceed 10% and fall bellow 20%, respectively of the coal ash. The kneading water rate is to be set around the plastic limit of coal ash. The duration of precuring and main precuring is to be 6 to 10h, at 30[degree]C and 10 to 15h at 60[degree]C, respectively. Explained is the result of mass production test with kneader, plastic former and crusher of the same structure as the presumed actual ones, and assessment test (laboratory test and field test on the road pavement) on the hardened and crushed ash with the compressive strength of 170kgf/cm[sup 2] as a pavement material. The present report also reports the operational start of a demonstration plant for the base material production. 5 refs., 11 figs., 2 tabs.

  8. Combustion and NOx emission characteristics with respect to staged-air damper opening in a 600 MWe down-fired pulverized-coal furnace under deep-air-staging conditions.

    Science.gov (United States)

    Kuang, Min; Li, Zhengqi; Wang, Zhihua; Jing, Xinjing; Liu, Chunlong; Zhu, Qunyi; Ling, Zhongqian

    2014-01-01

    Deep-air-staging combustion conditions, widely used in tangential-fired and wall-arranged furnaces to significantly reduce NOx emissions, are premature up to now in down-fired furnaces that are designed especially for industry firing low-volatile coals such as anthracite and lean coal. To uncover combustion and NOx emission characteristics under deep-air-staging conditions within a newly operated 600 MWe down-fired furnace and simultaneously understand the staged-air effect on the furnace performance, full-load industrial-size measurements taken of gas temperatures and species concentrations in the furnace, CO and NOx emissions in flue gas, and carbon in fly ash were performed at various staged-air damper openings of 10%, 20%, 30%, and 50%. Increasing the staged-air damper opening, gas temperatures along the flame travel (before the flame penetrating the staged-air zone) increased initially but then decreased, while those in the staged-air zone and the upper part of the hopper continuously decreased and increased, respectively. On opening the staged-air damper to further deepen the air-staging conditions, O2 content initially decreased but then increased in both two near-wall regions affected by secondary air and staged air, respectively, whereas CO content in both two regions initially increased but then decreased. In contrast to the conventional understanding about the effects of deep-air-staging conditions, here increasing the staged-air damper opening to deepen the air-staging conditions essentially decreased the exhaust gas temperature and carbon in fly ash and simultaneously increased both NOx emissions and boiler efficiency. In light of apparently low NOx emissions and high carbon in fly ash (i.e., 696-878 mg/m(3) at 6% O2 and 9.81-13.05%, respectively) developing in the down-fired furnace under the present deep-air-staging conditions, further adjustments such as enlarging the staged-air declination angle to prolong pulverized-coal residence times in the

  9. Techniques to determine ignition, flame stability and burnout of blended coals in p.f. power station boilers

    Energy Technology Data Exchange (ETDEWEB)

    Su, S.; Pohl, J.H.; Holcombe, D.; Hart, J.A. [University of Queensland, Brisbane, Qld. (Australia). Dept. of Chemical Engineering

    2001-07-01

    The blending of coals has become popular to improve the performance of coals, to meet specifications of power plants and to reduce the cost of coals. This article reviews the results and provides new information on ignition, flame stability, and carbon burnout studies of blended coals. The reviewed studies were conducted in laboratory-, pilot-, and full-scale facilities. The new information was taken in pilot-scale studies. The results generally show that blending a high-volatile coal with a low-volatile coal or anthracite can improve the ignition, flame stability and burnout of the blends. This paper discusses two general methods to predict the performance of blended coals: (1) experiment; and (2) indices. Laboratory- and pilot-scale tests, at least, provide a relative ranking of the combustion performance of coal/blends in power station boilers. Several indices, volatile matter content, heating value and a maceral index, can be used to predict the relative ranking of ignitability and flame stability of coals and blends. The maceral index, fuel ratio, and vitrinite reflectance can also be used to predict the absolute carbon burnout of coal and blends within limits. 59 refs., 20 figs., 4 tabs.

  10. Capital and operating costs for industrial boilers. Final report Apr-Jun 79

    Energy Technology Data Exchange (ETDEWEB)

    Gibbs, L.L.; AbrahaM, J.P.; Noe, N.D.; Forste, D.S.; Kimball, H.T.

    1979-06-01

    The report provides estimates of capital and operating costs for industrial boilers. Costs are related to the type of fuel fired, firing design and rated capacity. Both package and field-erected boilers are evaluated. Fuels considered include coal, residual oil, distillate oil and natural gas. Firing designs for coal include underfeed-stoker, spreader-stoker and pulverized. Rated capacities range from 15(10 to the 6th)Btu/hr for oil and gas to 700(10 to the 6th)Btu/hr for coal. Costs are developed on a study estimate basis. Individual boiler cost estimates were plotted and cost equations developed for total equipment, installation (direct and indirect) and operating costs (variable and fixed).

  11. Operation of flue gas fan during mixed burning of bituminous coal in a lean coal-fired boiler:problems and solutions%贫煤锅炉掺烧烟煤热炉烟风机运行问题及其解决措施

    Institute of Scientific and Technical Information of China (English)

    张兴豪; 范庆伟; 张立欣

    2014-01-01

    介绍了华能南京电厂贫煤锅炉的抽炉烟干燥技术,分析了该锅炉掺烧烟煤后热炉烟风机磨损、积灰、振动、出力不足等问题。对此,通过对热炉烟风机实施选型优化、叶片防磨治理、合理安排检修等措施后,大大延长了热炉烟风机使用周期和寿命,减少了检修时间和检修费用,保证了贫煤锅炉掺烧烟煤制粉系统的安全性和可靠性。%The flue gas drying technology implemented in lean coal-fired boiler of Nanj ing Power Plant was introduced.Problems such as hot flue gas fan abrasion,deposited ash vibrancy,and insufficient output oc-curred on this boiler were investigated.Moreover,solutions for the above problems were put forward. Through fan type selection optimization,fan blade abrasion resistant treatment,reasonable arrangement of maintenance and other measures,the problems of fan blade abrasion and deposited ash vibrancy were well solved,and the service life of flue gas fan was significantly prolonged,the time and cost of maintenance were reduced,and the safety and reliability of bituminous coal pulverizing system in lean coal-fired boiler were ensured.

  12. High Temperature Behavior of Cr3C2-NiCr Coatings in the Actual Coal-Fired Boiler Environment

    Science.gov (United States)

    Bhatia, Rakesh; Sidhu, Hazoor Singh; Sidhu, Buta Singh

    2015-03-01

    Erosion-corrosion is a serious problem observed in steam-powered electricity generation plants, and industrial waste incinerators. In the present study, four compositions of Cr3C2-(Ni-20Cr) alloy coating powder were deposited by high-velocity oxy-fuel spray technique on T-91 boiler tube steel. The cyclic studies were performed in a coal-fired boiler at 1123 K ± 10 K (850 °C ± 10 °C). X-ray diffraction, scanning electron microscopy/energy dispersive X-ray analysis and elemental mapping analysis techniques were used to analyze the corrosion products. All the coatings deposited on T-91 boiler tube steel imparted hot corrosion resistance. The 65 pctCr3C2 -35 pct (Ni-20Cr)-coated T-91 steel sample performed better than all other coated samples in the given environment.

  13. Evaluation of the behavior of shrouded plasma spray coatings in the platen superheater of coal-fired boilers

    Science.gov (United States)

    Sidhu, Buta Singh; Prakash, S.

    2006-06-01

    Nickel- and cobalt-based coatings were formulated by a shrouded plasma spray process on boiler tube steels, namely, ASTM-SA210-grade A1 (GrA1), ASTM-SA213-T-11 (T11), and ASTM-SA213-T-22 (T22). The Ni-22Cr-10Al-1Y alloy powder was sprayed as a bond in each case before the final coating. The degradation behavior of the bared and coated steels was studied in the platen superheater of the coal-fired boiler. The samples were inserted through the soot blower dummy points with the help of stainless steel wires. The coatings were found to be effective in increasing resistance to degradation in the given boiler environment. The maximum protection was observed in the case of Stellite-6 (St-6) coating.

  14. Evaluation of the behavior of shrouded plasma spray coatings in the platen superheater of coal-fired boilers

    Energy Technology Data Exchange (ETDEWEB)

    Sidhu, B.S.; Prakash, S. [GZS College of Engineering & Technology, Bathinda (India). Dept. of Mechanical Engineering

    2006-06-15

    Nickel- and cobalt-based coatings were formulated by a shrouded plasma spray process on boiler tube steels, namely, ASTM-SA210-grade A1 (GrA1), ASTM-SA213-T-11 (T11), and ASTM-SA213-T-22 (T22). The Ni-22Cr-10A1-1Y alloy powder was sprayed as a bond in each case before the final coating. The degradation behavior of the bared and coated steels was studied in the platen superheater of the coal-fired boiler. The samples were inserted through the soot blower dummy points with the help of stainless steel wires. The coatings were found to be effective in increasing resistance to degradation in the given boiler environment. The maximum protection was observed in the case of Stellite-6 (St-6) coating.

  15. Erosion in Steam General Tubes in Boiler and ID Fans in Coal Fired FBC Power Plant

    Directory of Open Access Journals (Sweden)

    Shaheen Aziz

    2012-01-01

    Full Text Available The FBC (Fluidized Bed Combustion is a technique used to make solid particles behave like fluid and grow very fast for the power generation using low grade coal. Due to its merits, first time this technology has been introduced in Pakistan by installing 3x50 MW power plants at Khanote. Fluidized beds have long been used for the combustion of low-quality, difficult fuels and have become a rapidly developing technology for the clean burning of coal. The FBC Power Plant at Khanote has been facing operational and technical problems, resulting frequently shut down of generation units, consequently facing heavy financial losses. This study reveals that due to the presence of high percentage of silica in the lime stone that are further distributed in the bottom ash, fly ash and re-injection material, the generation tubes in the boiler and wings/blades of ID (Induced Draft fans were eroded. In addition, filter bags were also ruptured; resulting frequent shut down of power plant units.

  16. Evaluation of activated carbon for control of mercury from coal-fired boilers

    Energy Technology Data Exchange (ETDEWEB)

    Miller, S.; Laudal, D.; Dunham, G. [Univ. of North Dakota, Grand Forks, ND (United States)

    1995-11-01

    The ability to remove mercury from power plant flue gas may become important because of the Clean Air Act amendments` requirement that the U.S. Environmental Protection Agency (EPA) assess the health risks associated with these emissions. One approach for mercury removal, which may be relatively simple to retrofit, is the injection of sorbents, such as activated carbon, upstream of existing particulate control devices. Activated carbon has been reported to capture mercury when injected into flue gas upstream of a spray dryer baghouse system applied to waste incinerators or coal-fired boilers. However, the mercury capture ability of activated carbon injected upstream of an electrostatic precipitator (ESP) or baghouse operated at temperatures between 200{degrees} and 400{degrees}F is not well known. A study sponsored by the U.S. Department of Energy and the Electric power Research Institute is being conducted at the University of North Dakota Energy & Environmental Research Center (EERC) to evaluate whether mercury control with sorbents can be a cost-effective approach for large power plants. Initial results from the study were reported last year. This paper presents some of the recent project results. Variables of interest include coal type, sorbent type, sorbent addition rate, collection media, and temperature.

  17. Principles of Selecting Type of Direct Flow Pulverized Coal Burner before Retrofit%直流煤粉燃烧器改造前的选型原则

    Institute of Scientific and Technical Information of China (English)

    李凤瑞

    2001-01-01

    针对锅炉燃烧器改造问题,提出在燃烧器改造前如何根据锅炉实际情况选择合适燃烧器类型的5项选型原则,包括煤种匹配原则、炉型匹配原则、工作业绩及创新性原则、经济性及安装检修方便性原则、运行自适应原则。对电厂煤粉燃烧器的改造有一定参考作用。%Which structure type of burner should be adopted for various utilities pulverized coal-fired boilers﹖ This paper puts forward five principles of selecting burner's type being of directive significance for the power plant that is going to retrofit burners.

  18. Efficiency of using direct-flow burners and nozzles in implementation of dry-bottom ash removal at the TPP-210A boiler furnace

    Science.gov (United States)

    Arkhipov, A. M.; Kanunnikov, A. A.; Kirichkov, V. S.; Prokhorov, V. B.; Fomenko, M. V.; Chernov, S. L.

    2017-02-01

    In reconstruction of operating pulverized coal-fired boilers, one of the main factors is the choice of a method for slag removal: dry bottom ash removal (DBAR) or slag-tap removal (STR). In this case, ecological and economic aspects should be taken into account, and also the early ignition of pulverized coal fuel, the reliability of operation of the furnace walls in the mode without slagging, and the stability of slag removal should be provided. In this work, issues of changeover of the pulverized coal-fired boilers of the TPP-210A type from the STR mode to the DBAR mode are considered. As of today, the main problems during the operation of these boilers are the high emissions of nitrogen oxides together with flue gases into the atmosphere and the appropriated payoffs, a small range of loads available, the necessity of stabilization of the pulverizedcoal flame sustainability by using the highly reactive fuel, large mechanical fuel underburning, etc. Results of studying aerodynamics of a furnace with DBAR obtained in the process of physical simulation are given; technical solutions and preliminary design (configuration of burners and nozzles in the boiler furnace, conceptual design of the pulverized coal burner, configuration of TPP-210A boiler with the low heat liberation of furnace cross-section and volumetric heat release) are set forth, which are associated with the optimization of aerodynamics of furnace volume, when the direct-flow burners and nozzles are used, and with organization of the efficient staged combustion of solid fuel. Two versions of possible modernization of a boiler unit are considered. Under conditions of the planned increase in the steam production capacity, the most promising measures are as follows: the DBAR implementation with reducing heat releases of the cross-section and volume of the furnace approximately by half, the installation of the direct-flow burners and nozzles with injection of recirculation gases into the active combustion

  19. Pulverizing System and Combustion System Performance Analysis of 300 MW Boiler%300MW锅炉制粉及燃烧系统性能分析

    Institute of Scientific and Technical Information of China (English)

    王伟; 蒋蓬勃; 赵锋

    2012-01-01

    Boiler #4 of a certain power plant is subcritical pressure once reheat controlled circulation boiler, design and production by shanghai boiler factory. In order to improve the operation economic, tap into the potential of energy-saving, process boiler combustion adjustment test. Through test and analysis to find out problems such as high ash carbon, low air preheater exchanger performance, and to provide the basis for power plant restructure.%某电厂4号锅炉为上海锅炉厂设计生产的亚临界压力一次中间再热控制循环汽包炉。为了提高机组运行经济性、挖掘节能潜力,对4号锅炉进行燃烧调整试验。通过试验分析其现存灰渣含碳量高、空预器换热性能低等问题,为电厂改造提供依据。

  20. Erosion-corrosion of plasma as sprayed and laser remelted Stellite-6 coatings in a coal fired boiler

    Energy Technology Data Exchange (ETDEWEB)

    Sidhu, B.S.; Prakash, S. [College of Engineering & Technology, Bathinda (India). Dept. of Mechanical Engineering

    2006-05-31

    Unacceptable levels of surface degradation of metal containment walls and heat exchanger tubing by a combined erosion-corrosion (E-C) mechanism have been experienced in some boilers. The recent use of coatings to protect the heat exchanger tubes of fluidized bed combustor from E-C problems has been suggested by many authors. The laser remelting of the surface coating is suggested as a promising technique to improve its physical properties. Aim of the present investigation is to evaluate the erosion-corrosion (E-C) behaviour of plasma as sprayed and laser remelted Stellite-6 (St-6) coatings on boiler tube steels in the actual coal fired boiler environment. The cyclic experimental studies were performed in the platen superheater zone of a coal fired boiler where the temperature was around 755{sup o}C and the study was carried out up to 10 cycles each of 100 h duration followed by 1 h cooling at ambient temperature. Coated steels were found to possess higher resistance to E-C than the uncoated steels. The highest degradation resistance has been indicated by the T11 steel coated and subsequently laser remelted.

  1. Chemical and physical properties of highly-loaded coal-water fuels and their effect on boiler performance

    Energy Technology Data Exchange (ETDEWEB)

    Farthing, G.A. Jr.; Daley, R.D.; Vecci, S.J.; Michaud, E.R.

    1983-01-01

    Coal-water fuels (CWF) are being developed as substitute fuels for industrial and utility boilers presently burning oil. The chemical and physical properties of CWF vary widely depending on the coal and preparation process used. Also, the traditional methods for characterizing fuels and existing correlations between boiler performance and fuel properties may not be applicable to CWF. Babcock and Wilcox is working under contract to the Electric Power Research Institute to determine the range of properties a CWF should have to qualify as a boiler fuel. Laboratory fuels characterization methods are being developed for use as standard procedures for measuring the key properties related to storage, atomization, combustion, handling in various transport systems, and deposition tendencies on boiler heat transfer surfaces. The relationship between laboratory-measured rheological characteristics of CWF's and their pipe flow and combustion performance is being determined. Atomization studies are being performed in a newly constructed atomization facility having the capability of testing atomizers at fuel flows equivalent to 5 to 50 million Btu/h. Atomization quality is assessed using laser diagnostics to determine droplet size and velocity distributions. Flame stability and combustion efficiency are being correlated with atomization quality through combustion testing at 5 x 10/sup 6/ Btu/h. The status of these studies is reported.

  2. Combining support vector regression and cellular genetic algorithm for multi-objective optimization of coal-fired utility boilers

    Energy Technology Data Exchange (ETDEWEB)

    Feng Wu; Hao Zhou; Tao Ren; Ligang Zheng; Kefa Cen [Zhejiang University, Hangzhou (China). State Key Laboratory of Clean Energy Utilization

    2009-10-15

    Support vector regression (SVR) was employed to establish mathematical models for the NOx emissions and carbon burnout of a 300 MW coal-fired utility boiler. Combined with the SVR models, the cellular genetic algorithm for multi-objective optimization (MOCell) was used for multi-objective optimization of the boiler combustion. Meanwhile, the comparison between MOCell and the improved non-dominated sorting genetic algorithm (NSGA-II) shows that MOCell has superior performance to NSGA-II regarding the problem. The field experiments were carried out to verify the accuracy of the results obtained by MOCell, the results were in good agreement with the measurement data. The proposed approach provides an effective tool for multi-objective optimization of coal combustion performance, whose feasibility and validity are experimental validated. A time period of less than 4 s was required for a run of optimization under a PC system, which is suitable for the online application. 19 refs., 8 figs., 2 tabs.

  3. PASSIVE CONTROL OF PARTICLE DISPERSION IN A PARTICLE-LADEN CIRCULAR JET USING ELLIPTIC CO-ANNULAR FLOW: A MEANS FOR IMPROVING UTILIZATION AND EMISSION REDUCTIONS IN PULVERIZED COAL BURNER

    Energy Technology Data Exchange (ETDEWEB)

    Ahsan R. Choudhuri

    2003-06-01

    A passive control technology utilizing elliptic co-flow to control the particle flinging and particle dispersion in a particle (coal)-laden flow was investigated using experimental and numerical techniques. Preferential concentration of particles occurs in particle-laden jets used in pulverized coal burner and causes uncontrollable NO{sub x} formation due to inhomogeneous local stoichiometry. This particular project was aimed at characterizing the near-field flow behavior of elliptic coaxial jets. The knowledge gained from the project will serve as the basis of further investigation on fluid-particle interactions in an asymmetric coaxial jet flow-field and thus is important to improve the design of pulverized coal burners where non-homogeneity of particle concentration causes increased NO{sub x} formation.

  4. Effects of moisture release and radiation properties in pulverized fuel combustion: A CFD modelling study

    DEFF Research Database (Denmark)

    Yin, Chungen

    2016-01-01

    Pulverized fuels (PF) prepared and fired in utility boilers always contain some moisture. For some fuels with high moisture contents (e.g., brown coals), the share of the evaporation enthalpy is quite significant compared to the heat released during combustion, which often needs to be reclaimed.......g., oxy-fuel or air–fuel), account for the variations in CO2 and H2O concentrations in a flame, and include the impacts of other participating gases (e.g., CO and hydrocarbons) needs to be derived for combustion CFD community....

  5. Deposit formation during coal-straw co-combustion in a utility PF-boiler

    Energy Technology Data Exchange (ETDEWEB)

    Hedebo Andersen, K.

    1998-08-01

    deposits could be taken as a smaller, but visually valid, representation of the boiler deposits in the superheating and reheating part. At 20% straw share, the probe deposits seem to represent an initial deposit necessary for build-up of the large mature deposits observed, but can not represent the mature deposits satisfactorily. CI was observed to primarily leave the boiler with the flue gas as gaseous HCI, and the CI-content in the probe and mature deposits was generally low (< 0,5 wt%). The corrosivity of the deposits due to CI is thus expected to be minor. The majority of K introduced with the straw was bonded as K-AI-silicate durring combustion, and the remaining available K formed K{sub 2}SO{sub 4}, which could participate in deposit formation and consolidation. No significant participation of K was seen in the coal ash deposits, whereas K was a large contributor to the up- and downstream probe deposits formed during co-combustion with 20% straw share, primarily as relatively small K-AI-silicate particles and as K{sub 2}SO{sub 4}. The deposition of sulphate could be related to the observed increase in deposit amount and tenacity with straw addition. The behaviour of K and CI from the straw is primarily controlled by the ash behaviour of the coal species. An evaluation of the shift from ash formation dominated by the coal ash species to ash formation dominated by the straw ash species (K-silicate and KCI) as a function of the straw share reveals, that the first major change is observed at 60% straw share, where KCI(cr,l) is observed at low temperatures. Based on these results, coal-straw co-combustion could thus be manageable also up to straw shares as high as 50% with regard to the deposits formed. The effect of coal-straw co-combustion on deposit formation in other utillity boilers was evaluated based upon the results from the experimental investigation at MKS1. Two major aspects were evaluated: The effect of flue gas temperatures and the effect of mixing. However

  6. Full Scale Deposition Trials at 150 MWe PF-boiler Co-firing COal and Straw: Summary of Results

    DEFF Research Database (Denmark)

    Andersen, Karin Hedebo; Frandsen, Flemming; Hansen, Peter Farkas Binderup

    1999-01-01

    . In the visual analysis, a significant increase in amount and tenacity of primarily the upstream deposit was observed as a function of increased straw share, exposure time and/or boiler load.The chemical analysis of the deposits suggest an increased participation of K and S in the formation of the deposits...... for the coal types utilised in the tests.The deposit formation observed during co-firing with up to 20% straw (energy basis), does not lead to fouling and slagging problems which cannot be overcome by increased sootblowing when firing the two coals used in the demonstration programme. However, slagging...

  7. Summary of workshop on materials issues in low emission boilers and high efficiency coal-fired cycles

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1997-12-01

    The purpose of the workshop was to review with experts in the field the materials issues associated with two of the primary coal power systems being developed by the DOE Office of Fossil Energy. The DOE-FE Advanced Power Systems Program includes natural gas-based and coal-based power systems. Major activities in the natural gas-based power systems area include the Advanced Turbine Systems (ATS) Program, the Fuel Cells Program, and Hybrid Cycles. The coal-based power systems projects include the Low Emissions Boiler Systems (LEBS) Program, the High-Performance Power Systems Program (HIPPS), the Integrated (Coal) Gasification Combined-Cycle Program, and the Fluidized-Bed Combustion Program. This workshop focused on the materials issues associated with the LEBS and HIPPS technologies.

  8. A collaborative project on the effects of coal quality on NO{sub x} emissions and carbon burnout in pulverised coal-fired utility boilers

    Energy Technology Data Exchange (ETDEWEB)

    Tilley, H.A.; O`Connor, M.; Stephenson, P.L.; Whitehouse, M.; Richards, D.G.; Hesselmann, G.; MacPhail, J.; Lockwood, F.C.; Williamson, J.; Williams, A.; Pourkashanian, M. [ETSU, Harwell (United Kingdom)

    1998-12-01

    This paper describes a UK Department of Trade and Industry-supported collaborative project entitled `The Effects of Coal Quality on Emission of Oxides of Nitrogen (NO{sub x}) and Carbon Burnout in Pulverised Coal-fired Utility Boilers`. The project involved extensive collaboration between the UK power generators, boiler and burner manufacturers and research groups in both industry and academia, together with several of the world`s leading computational fluid dynamics (CFD) `software houses`. The prime objectives of the project were to assess the relationship between NO{sub x} emissions and carbon burnout and to develop and validate predictive tools for assessing coals. Experimental work was carried out on various laboratory-scale apparatus and on single burner test facilities ranging from 160 kW{sub th} to 40 MW{sub th} in size and measurements were obtained from full-scale 500 MW{sub e} utility boiler trials. This data and basic coal data were then used to develop mathematical models to predict full-scale boiler performance with respect to NO{sub x} emissions and carbon-in-ash. Results showed good correlations for NO{sub x} and carbon burnout when comparing data from full-scale and large-scale rig trials. Laboratory-scale tests were found to be useful but the influence of burner aerodynamics was more difficult to quantify. Modelling showed that predicted NO{sub x} emissions were encouragingly close to measured emissions but predicting carbon burnout was less successful. 24 refs., 4 figs., 6 tabs.

  9. Bergemann lance-type water blowers for coal boilers; Bergemann-Wasserlanzenblaeser fuer Kohlekessel

    Energy Technology Data Exchange (ETDEWEB)

    Bartels, F.; Weber, H.G.

    1995-12-31

    Residues from coal combustion create considerable problems for boilers. Slag and ashes on heating surfaces have a negative influence on steam generator efficiency and reduce boiler cycles. If different types of coal are used there are not only specific demands for stable furnace operation but problems of slag control at the different steam generator surfaces. Vaporiser heating surfaces of combustion chambers show extra-tough slag which can not always be removed by steam or air blowers. Forty years ago one therefore started using water as an alternative cleaning agent. At first, hand-held lances were used. Due to its high kinetic energy, water jets penetrate the pores of the slag layers on the vaporiser pipes where it evaporates and makes the slag pop off due to the sudden considerable increase in volume. These results consequently lead to the mechanisation of water-blowing as early as the 1950s; steam soot blowers were retrofitted for water. The Bergemann company used its own system of wall-blowers and improved the water blowing technology with the help of RWE by testing the technology under real life conditions in one or RWE`s lignite power stations. (orig.) [Deutsch] Rueckstaende aus der Verbrennung von Kohle-Brennstoffen fuehren beim Betrieb von Kesselanlagen zu erheblichen Problemen. Der Wirkungsgrad der Dampferzeuger wird durch zum Teil hartnaeckige Ansaetze von Schlacken und Aschen auf den Heizflaechen negativ beeinflusst und die Kessel-Reisezeit herabgesetzt. Besonders die Verbrennung von verschiedenen Kohlearten mit einem breiten Brennstoffband fuehrt neben spezifischen Anforderungen an den stabilen Feuerungsbetrieb vor allem auch zu den Fragen der Beherrschung von Verschlackungen an den unterschiedlichen Dampferzeugerheizflaechen. An den Verdampferheizflaechen der Brennkammern koennen besonders hartnaeckige Verschlackungen auftreten, die mit Dampf und Luft als Blasmedium nicht immer zu entfernen sind. Wasser wurde deshalb als alternatives Reinigungsmedium

  10. Two-in-one fuel combining sugar cane with low rank coal and its CO₂ reduction effects in pulverized-coal power plants.

    Science.gov (United States)

    Lee, Dong-Wook; Bae, Jong-Soo; Lee, Young-Joo; Park, Se-Joon; Hong, Jai-Chang; Lee, Byoung-Hwa; Jeon, Chung-Hwan; Choi, Young-Chan

    2013-02-05

    Coal-fired power plants are facing to two major independent problems, namely, the burden to reduce CO(2) emission to comply with renewable portfolio standard (RPS) and cap-and-trade system, and the need to use low-rank coal due to the instability of high-rank coal supply. To address such unresolved issues, integrated gasification combined cycle (IGCC) with carbon capture and storage (CCS) has been suggested, and low rank coal has been upgraded by high-pressure and high-temperature processes. However, IGCC incurs huge construction costs, and the coal upgrading processes require fossil-fuel-derived additives and harsh operation condition. Here, we first show a hybrid coal that can solve these two problems simultaneously while using existing power plants. Hybrid coal is defined as a two-in-one fuel combining low rank coal with a sugar cane-derived bioliquid, such as molasses and sugar cane juice, by bioliquid diffusion into coal intrapores and precarbonization of the bioliquid. Unlike the simple blend of biomass and coal showing dual combustion behavior, hybrid coal provided a single coal combustion pattern. If hybrid coal (biomass/coal ratio = 28 wt %) is used as a fuel for 500 MW power generation, the net CO(2) emission is 21.2-33.1% and 12.5-25.7% lower than those for low rank coal and designed coal, and the required coal supply can be reduced by 33% compared with low rank coal. Considering high oil prices and time required before a stable renewable energy supply can be established, hybrid coal could be recognized as an innovative low-carbon-emission energy technology that can bridge the gulf between fossil fuels and renewable energy, because various water-soluble biomass could be used as an additive for hybrid coal through proper modification of preparation conditions.

  11. Mercury speciation and distribution in a 660-megawatt utility boiler in Taiwan firing bituminous coals.

    Science.gov (United States)

    Hsi, Hsing-Cheng; Lee, Hsiu-Hsia; Hwang, Jyh-Feng; Chen, Wang

    2010-05-01

    Mercury speciation and distribution in a 660-MW tangential-fired utility boiler in Taiwan burning Australian and Chinese bituminous coal blends was investigated. Flue gases were simultaneously sampled at the selective catalytic reduction (SCR) inlet, the SCR outlet, the electrostatic precipitator (ESP) outlet, and the stack. Samplings of coal, lime, bottom ash/slag, fly ash, and gypsum slurry were also conducted. Results indicated that flue gases at the inlet to SCR contained a great potion of particle-bound mercury (Hg(p)), 59-92% of the total mercury. Removal of mercury was not observed for the SCR system. However, repartitioning of mercury species across the SCR occurred that significantly increased the portion of elemental mercury (Hg0) to up to 29% and oxidized mercury (Hg2+) to up to 33% in the SCR outlet gas. Overreporting of Hg(p) at the inlet of SCR may cause the observed repartitioning; the high ammonia/nitric oxide circumstance in the SCR unit was also speculated to cause the mercury desorption from ash particles and subsequent reentrance into the gas phase. ESP can remove up to 99% of Hg(p), and wet flue gas desulfurization (FGD) can remove up to 84% of Hg2+. Mercury mass balances were calculated to range between 81 and 127.4%, with an average of 95.7% wherein 56-82% was in ESP fly ash, 8.7-18.6% was retained in the FGD gypsum, and 6.2-26.1% was emitted from the stack. Data presented here suggest that mercury removal can be largely enhanced by increasing the conversion of Hg0 into Hg(p) and Hg2+.

  12. Effect of large aspect ratio of biomass particles on carbon burnout in a utility boiler

    Energy Technology Data Exchange (ETDEWEB)

    D. Gera; M.P. Mathur; M.C. Freeman; Allen Robinson [Fluent, Inc./NETL, Morgantown, WV (United States)

    2002-12-01

    This paper reports on the development and validation of comprehensive combustion sub models that include the effect of large aspect ratio of biomass (switchgrass) particles on carbon burnout and temperature distribution inside the particles. Temperature and carbon burnout data are compared from two different models that are formulated by assuming (i) the particles are cylindrical and conduct heat internally, and (ii) the particles are spherical without internal heat conduction, i.e., no temperature gradient exists inside the particle. It was inferred that the latter model significantly underpredicted the temperature of the particle and, consequently, the burnout. Additionally, some results from cofiring biomass (10% heat input) with pulverized coal (90% heat input) are compared with the pulverized coal (100% heat input) simulations and coal experiments in a tangentially fired 150 MW{sub e} utility boiler. 26 refs., 7 figs., 4 tabs.

  13. Co-firing of coal with biomass and waste in full-scale suspension-fired boilers

    Energy Technology Data Exchange (ETDEWEB)

    Dam-Johansen, Kim; Frandsen, Flemming J.; Jensen, Peter A.; Jensen, Anker D. [Technical Univ. of Denmark, Lyngby (Denmark). Dept. of chemical and Biochemical Engineering

    2013-07-01

    The energy policy in Denmark has for many years focused on lowering the net CO{sub 2} emission from heat and power production by replacing fossil fuels by renewable resources. This has been done by developing dedicated grate-fired boilers for biomass and waste fuels but also by developing coal-based suspension-fired boilers to accept still higher fractions of biomass or waste material as fuels. This last development has been challenging of many reasons, including pre-treatment of fuels, and solving potential emission and operational problems during the simultaneous development of supercritical steam cycles with steam temperatures close to 600 C, providing power efficiencies close to 50% (Hein KRG, Sustainable energy supply and environment protection - strategies, resources and technologies. In: Gupta R, Wall T, Hupa M, Wigley F, Tillman D, Frandsen FJ (eds) Proceedings of international conference on impact of fuel quality on power production and the environment, Banff Conference Centre, Banff, Alberta, Canada, 29 Sept-4 Oct, 2008). For 25 years the CHEC (Combustion and Harmful Emission Control) Research Centre at DTU Chemical Engineering, has attained a leading role in research, supporting power producing industry, plant owners and boiler manufacturers to optimize design and operation and minimize cost and environmental impact using alternative fuels in suspension fired boilers. Our contribution has been made via a combination of full-scale measuring campaigns, pilot-scale studies, lab-scale measurements and modeling tools. The research conducted has addressed many issues important for co-firing, i.e. fuel processing, ash induced boiler deposit formation and corrosion, boiler chamber fuel conversion and emission formation, influence on flue gas cleaning equipment and the utilization of residual products. This chapter provides an overview of research activities, aiming at increasing biomass shares during co-firing in suspension, conducted in close collaboration with

  14. Deposit Formation in a 150 MWe Utility PF-Boiler during Co-combustion of Coal and Straw

    DEFF Research Database (Denmark)

    Andersen, Karin Hedebo; Frandsen, Flemming; Hansen, P. F. B.

    2000-01-01

    the small ones was observed. No chlorine species was observed in the deposits collected, and selective chlorine corrosion is therefore not expected to constitute a problem in co-combustion of coal and straw up to 20% straw share, for the coal types utilized in the tests. However, deposition problems could...... (SEM) combined with energy dispersive X-ray analyses (SEM-EDX) and bulk chemical analyses. In the visual analysis, a significant increase in the amount and tenacity of the upstream deposits was observed as a function of increased straw share, exposure time, and boiler load. The chemical analyses...... problematic deposits. Go-firing straw also caused a change in the structure of the upstream deposits. During coal combustion an ordered, "finger" structure of the larger particles with small particles between was observed, whereas during co-combustion a more random deposition of the larger particles among...

  15. Studies of the fate of sulfur trioxide in coal-fired utility boilers based on modified selected condensation methods.

    Science.gov (United States)

    Cao, Yan; Zhou, Hongcang; Jiang, Wu; Chen, Chien-Wei; Pan, Wei-Ping

    2010-05-01

    The formation of sulfur trioxide (SO(3)) in coal-fired utility boilers can have negative effects on boiler performance and operation, such as fouling and corrosion of equipment, efficiency loss in the air preheater (APH), increase in stack opacity, and the formation of PM(2.5). Sulfur trioxide can also compete with mercury when bonding with injected activated carbons. Tests in a lab-scale reactor confirmed there are major interferences between fly ash and SO(3) during SO(3) sampling. A modified SO(3) procedure to maximize the elimination of measurement biases, based on the inertial-filter-sampling and the selective-condensation-collecting of SO(3), was applied in SO(3) tests in three full-scale utility boilers. For the two units burning bituminous coal, SO(3) levels starting at 20 to 25 ppmv at the inlet to the selective catalytic reduction (SCR), increased slightly across the SCR, owing to catalytic conversion of SO(2) to SO(3,) and then declined in other air pollutant control device (APCD) modules downstream to approximately 5 ppmv and 15 ppmv at the two sites, respectively. In the unit burning sub-bituminous coal, the much lower initial concentration of SO(3) estimated to be approximately 1.5 ppmv at the inlet to the SCR was reduced to about 0.8 ppmv across the SCR and to about 0.3 ppmv at the exit of the wet flue gas desulfurization (WFGD). The SO(3) removal efficiency across the WFGD scrubbers at the three sites was generally 35% or less. Reductions in SO(3) across either the APH or the dry electrostatic precipitator (ESP) in units burning high-sulfur bituminous coal were attributed to operating temperatures being below the dew point of SO(3).

  16. Development of Square Coal Tube in Boiler%方型锅炉落煤筒的研制

    Institute of Scientific and Technical Information of China (English)

    高平; 王婵; 郭在在; 付利涛; 兰兰; 邸建辉; 闫志飞; 田迎春; 郭永亮

    2014-01-01

    Aimed at the reasons for the early deformation in service and cracking failure of the welding-manufactured square tubes in coal boiler,a lost foam casting process scheme for the square tubes in coal boiler was put forward,and some measures were adopted,such as designing a "well" shape deformation brace,increasing casting chamfering radius,adjusting chemical composition of the material,and so on.The production process for the square tubes in coal boiler were introduced,including lost foam casting process,melting and pouring process,model making and coating process,and model packing process.Practice proves that the service life of the cast square tubes is 1.6 times of welding tubes,which effectively improve the efficiency of transporting coal and the enterprise economic benefit.%针对焊接制造锅炉落煤筒服役早期出现变形和开裂失效的原因,提出了消失模铸造落煤筒的方案,并采取了设计“井”形防变形拉筋,加大铸件铸造倒角半径,调整优化材料的化学成分等措施.同时介绍了消失模铸造落煤筒的熔炼、浇注、模型制作、涂料涂刷和模型装箱等工艺.实践证明,研制的落煤筒使用寿命是焊接制造的1.6倍,有效地提高输煤效率和企业的经济效益.

  17. CO-FIRING COAL: FEEDLOT AND LITTER BIOMASS (CFB AND CLB) FUELS IN PULVERIZED FUEL AND FIXED BED BURNERS

    Energy Technology Data Exchange (ETDEWEB)

    Kalyan Annamalai; John Sweeten; Saqib Mukhtar; Ben Thein; Gengsheng Wei; Soyuz Priyadarsan; Senthil Arumugam; Kevin Heflin

    2003-08-28

    Intensive animal feeding operations create large amounts of animal waste that must be safely disposed of in order to avoid environmental degradation. Cattle feedlots and chicken houses are two examples. In feedlots, cattle are confined to small pens and fed a high calorie grain-diet diet in preparation for slaughter. In chicken houses, thousands of chickens are kept in close proximity. In both of these operations, millions of tons of manure are produced every year. The manure could be used as a fuel by mixing it with coal in a 90:10 blend and firing it in an existing coal suspension fired combustion systems. This technique is known as co-firing, and the high temperatures produced by the coal will allow the biomass to be completely combusted. Reburn is a process where a small percentage of fuel called reburn fuel is injected above the NO{sub x} producing, conventional coal fired burners in order to reduce NO{sub x}. The manure could also be used as reburn fuel for reducing NO{sub x} in coal fired plants. An alternate approach of using animal waste is to adopt the gasification process using a fixed bed gasifier and then use the gases for firing in gas turbine combustors. In this report, the cattle manure is referred to as feedlot biomass (FB) and chicken manure as litter biomass (LB). The report generates data on FB and LB fuel characteristics. Co-firing, reburn, and gasification tests of coal, FB, LB, coal: FB blends, and coal: LB blends and modeling on cofiring, reburn systems and economics of use of FB and LB have also been conducted. The biomass fuels are higher in ash, lower in heat content, higher in moisture, and higher in nitrogen and sulfur (which can cause air pollution) compared to coal. Small-scale cofiring experiments revealed that the biomass blends can be successfully fired, and NO{sub x} emissions will be similar to or lower than pollutant emissions when firing coal. Further experiments showed that biomass is twice or more effective than coal when

  18. 700-MW coal fired sliding pressure operation boiler with improving operational characteristics. ; Chubu Electric Power Co. Inc. Hekinan thermal power station

    Energy Technology Data Exchange (ETDEWEB)

    Matsuda, J.; Kiyama, K. (Babcock-Hitachi K.K., Tokyo (Japan))

    1993-02-01

    In response to requirements of improvements of efficiency and operability to provide demand control and environmental preservation in coal fired boilers, Babcock-Hitachi has endeavored to develop a large capacity coal fired boiler. As a result, Babcock-Hitachi has installed a 700MW supercritical sliding pressure operation coal fired once through boiler at the Hekinan Thermal Power Station Unit No.2 of Chubu Electric Power Co. For this coal fired boiler, spiral water wall construction was adopted to stabilize the furnace outlet water temperature via uniform heat absorption at the furnace. A three-stage spray-type attemperator was also applied to the main steam temperature control to improve load controllability and to correspond to a fluctuation of heat absorption at the furnace and the convection pass zone. Moreover, gas recirculation system, parallel gas damper, and intermediate spray attemperator were used to control the reheat steam temperature. The present article describes design summary and results of trial operation of this large capacity coal fired boiler. 11 figs., 3 tabs.

  19. Kinetic analysis of single-particle pulverized coal during high-gradient magnetic separation%高梯度磁选中单颗粒微粉煤的动力学分析

    Institute of Scientific and Technical Information of China (English)

    刘鹏; 焦红光

    2012-01-01

    为了建立气固流态化磁选过程中颗粒群的相互作用模型,优化了高梯度磁选设备工作参数,在单颗粒微粉煤比磁化率一定的条件下,通过对高梯度磁选中单颗粒球形微粉煤的动力学分析,建立了气固流态化分选过程中的单颗粒煤粉运动的动态数学模型;进而探索出聚磁介质当量直径的临界模型,并分析了单颗粒微粉煤被捕集到聚磁介质上时相对气体流速的运动速度。%To establish the model of granule group interaction during gas-solid fluidization magnetic separa- tion, the paper optimized the operation parameters of the high-gradient magnetic separation equipment. On thecondition of keeping the specific magnetic susceptibility constant, through kinetic analysis of the spherical sin- gle-particle pulverized coal during high-gradient magnetic separation, a dynamic mathematical model of single- particle pulverized coal during gas-solid fluidization magnetic separation was established. And then the critical model of the equivalent diameter of the magnetic medium was achieved. Finally the relative gas flow velocity of single-particle pulverized coal was analyzed when single-particle pulverized coal was trapped onto the mag- netic medium.

  20. Advances in control of PM{sub 2.5} and PM{sub 2.5} precursors generated by the combustion of pulverized coal

    Energy Technology Data Exchange (ETDEWEB)

    Miller, C.A.; Srivastava, R.K.; Sedman, C.B. [US Environmental Protection Agency, Triangle Park, NC (United States). Office of Research and Development

    2002-07-01

    Particulate matter smaller than 2.5 {mu}m in aerodynamic diameter (PM{sub 2.5}) from coal-fired boilers is composed of directly emitted (primary) particles and particles formed from precursors (secondary particles). Technologies to reduce emissions of precursors to secondary PM{sub 2.5} emitted by coal-fired utility plants include wet and dry flue gas desulphurization (FGD). Limestone forced oxidation (LSFO) systems are the predominant wet FGD technology in use, and lime spray dryers (LSDs) represent the predominant dry FGD systems. A predictive model indicates that LSD systems have low annualized costs than LSFO systems for coals with less than 2% sulphur and for plants smaller than 300 MWe. Control technologies for primary PM{sub 2.5} include hybrid systems such as the combined hybrid particulate control system and an electrostatically enhanced fabric filter (ESFF) system. The ESFF can provide improved PM{sub 2.5} collection and lower fan power requirements compared to a conventional pulse-jet baghouse. There is a brief discussion of potential multi-pollutant control of mercury. 29 refs., 5 figs., 3 tabs.

  1. TOXECON RETROFIT FOR MERCURY AND MULTI-POLLUTANT CONTROL ON THREE 90 MW COAL FIRED BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    Richard E. Johnson

    2004-07-30

    With the Nation's coal-burning utilities facing tighter controls on mercury pollutants, the U.S. Department of Energy is supporting projects that could offer power plant operators better ways to reduce these emissions at much lower costs. Sorbent injection technology represents one of the simplest and most mature approaches to controlling mercury emissions from coal-fired boilers. It involves injecting a solid material such as powdered activated carbon into the flue gas. The gas-phase mercury in the flue gas contacts the sorbent and attaches to its surface. The sorbent with the mercury attached is then collected by a particle control device along with the other solid material, primarily fly ash. WE Energies has over 3,700 MW of coal-fired generating capacity and supports an integrated multi-emission control strategy for SO{sub 2}, NO{sub x} and mercury emissions while maintaining a varied fuel mix for electric supply. The primary goal of this project is to reduce mercury emissions from three 90 MW units that burn Powder River Basin coal at the WE Energies Presque Isle Power Plant. Additional goals are to reduce nitrogen oxide (NO{sub x}), sulfur dioxide (SO{sub 2}), and particulate matter (PM) emissions, allow for reuse and sale of fly ash, demonstrate a reliable mercury continuous emission monitor (CEM) suitable for use in the power plant environment, and demonstrate a process to recover mercury captured in the sorbent. To achieve these goals, WE Energies (the Participant) will design, install, and operate a TOXECON{trademark} (TOXECON) system designed to clean the combined flue gases of units 7, 8, and 9 at the Presque Isle Power Plant. TOXECON is a patented process in which a fabric filter system (baghouse) installed down stream of an existing particle control device is used in conjunction with sorbent injection for removal of pollutants from combustion flue gas. For this project, the flue gas emissions will be controlled from the three units using a single

  2. Numerical investigation of full scale coal combustion model of tangentially fired boiler with the effect of mill ducting

    Energy Technology Data Exchange (ETDEWEB)

    Achim, Daniela [Monash University, Department of Chemical Engineering, Clayton, VIC (Australia); Naser, J.; Morsi, Y.S. [Swinburne University of Technology, Faculty of Engineering and Industrial Sciences, Hawthorn, VIC (Australia); Pascoe, S. [Yallourn Energy, Moe, VIC (Australia)

    2009-11-15

    In this paper a full scale combustion model incorporating upstream mill ducting of a large tangentially fired boiler with flue gas recirculation was examined numerically. Lagrangian particle tracking was used to determine the coal particle paths and the Eddy Dissipation Model for the analysis of the gas phase combustion. Moreover volatiles and gaseous char products, given off by the coal particles were modelled by Arrhenius single phase reactions and a transport equation was solved for each material given off by the particles. Thermal, prompt, fuel and reburn NO{sub x} models with presumed probability density functions were used to model NO{sub x} production and the discrete transfer radiation model was used to model radiation heat transfer. Generally, the findings indicated reasonable agreement with observed qualitative and quantitative data of incident heat flux on the walls. The model developed here could be used for a range of applications in furnace design and optimisation of gas emissions of coal fired boiler plants. (orig.)

  3. Demonstration of SCR technology for the control of NOx emissions from high-sulfur coal-fired utility boilers

    Energy Technology Data Exchange (ETDEWEB)

    Hinton, W.S. [W.S. Hinton and Associates, Cantonment, FL (United States); Maxwell, J.D.; Healy, E.C.; Hardman, R.R. [Southern Company Services, Inc., Birmingham, AL (United States); Baldwin, A.L. [Dept. of Energy, Pittsburgh, PA (United States)

    1997-12-31

    This paper describes the completed Innovative Clean Coal Technology project which demonstrated SCR technology for reduction of flue gas NO{sub x} emissions from a utility boiler burning US high-sulfur coal. The project was sponsored by the US Department of Energy, managed and co-funded by Southern Company Services, Inc. on behalf of the Southern Company, and also co-funded by the Electric Power Research Institute and Ontario Hydro. The project was located at Gulf Power Company`s Plant Crist Unit 5 (a 75 MW tangentially-fired boiler burning US coals that had a sulfur content ranging from 2.5--2.9%), near Pensacola, Florida. The test program was conducted for approximately two years to evaluate catalyst deactivation and other SCR operational effects. The SCR test facility had nine reactors: three 2.5 MW (5,000 scfm), and operated on low-dust flue gas. The reactors operated in parallel with commercially available SCR catalysts obtained from suppliers throughout the world. Long-term performance testing began in July 1993 and was completed in July 1995. A brief test facility description and the results of the project are presented in this paper.

  4. Studies on the effect of coal properties on pulverised coal fired boiler performance operating with advanced low NO{sub x} technologies

    Energy Technology Data Exchange (ETDEWEB)

    Morgan, D.J.; Kamp, W.L. van de [International Flame Research Foundation, IJmuiden (Netherlands)

    1998-12-31

    Reburning or fuel staging is a technology that can be applied as a retro-fit to burners as a means of reducing NO{sub x} emissions. This report concentrates on using existing knowledge of reburning techniques, with the aim of developing an Integrated Fuel Staged Burner whereby the reburning fuel can be introduced within the burner itself. The investigations were conducted in a simulated boiler chamber with internal dimensions of 2 x 2 x 6.3 m. The single burner experiments were performed with Gottelborn (HVB), El Cerejon (HVB), Middelburg (MVB), Klein Kopje (MVB) and Polish coal (HVB). The experiments were conducted at the scale of 2.5 MW{sub t} with a swirl stabilised Internally Fuel Staged Burner (IFSB). The primary fuel was a bituminous coal of either high or medium volatile content and the reburning fuels were natural gas or a bituminous coal, again with a high or medium volatile content. The reburn fuel fraction varied from 0% to 40% on a fuel input basis. The main parameters affecting emissions of NO{sub x} and burnout were the primary zone stoichiometry, reburn fuel fraction, tertiary air position, coal type and flame type. With reburning conditions of 20% gas (reburn fuel)/80% coal (primary fuel) NO{sub x} could be reduced in the range 55 to {approximately} 78%, relative to a baseline 100% coal flame, depending on the location of the tertiary air and coal type. Coal over coal reburning led to reduced concentrations of NO{sub x} relative to the baseline flames, but increased concentrations compared to conditions where natural gas was used as the reburn fuel, which is consistent with the higher concentration of fuel-bound nitrogen. 16 refs., 22 figs., 7 tabs.

  5. Evaluation of Biomass and Coal Briquettes for a Spreader Stoker Boiler Using an Experimental Furnace --- Modeling and Test

    Science.gov (United States)

    Wiggins, Gavin Memminger

    The compliance of coal-fired boilers with emissions regulations is a concern for many facilities. The introduction of biomass briquettes in industrial boilers can help to reduce greenhouse gas emissions and coal usage. In this research project, a thermodynamic chemical equilibrium model was derived and analytical simulations performed for a coal boiler system for several types of biomass fuels such as beech, hickory, maple, poplar, white oak, willow, sawdust, torrefied willow, and switchgrass. The biomass emissions were compared to coal and charcoal emissions. The chemical equilibrium analysis numerically estimated the emissions of CO, CO2, NO, NO2, N 2O, SO2, and SO3. When examining the computer results, coal and charcoal emitted the highest CO, CO2, and SO x levels while the lowest (especially for SOx) were reached by the biomass fuels. Similarly, NOx levels were highest for the biomass and lowest for coal and charcoal. To validate these analytical results, a custom traveling grate furnace was designed and fabricated to evaluate different types of biofuels in the laboratory for operation temperatures and emissions. The furnace fuels tested included coal, charcoal, torrefied wood chips, and wood briquettes. As expected, the coal reached the highest temperature while the torrefied wood chips offered the lowest temperature. For CO and NO x emissions, the charcoal emitted the highest levels while the wood briquettes emitted the lowest levels. The highest SO2 emissions were reached by the coal while the lowest were emitted by the wood briquettes. When compared to the coal fuel, charcoal emissions for CO increased by 103%, NO and NOx decreased by 21% and 20% respectively, and SO2 levels decreased by 92%. For torrefied wood, emissions for CO increased by 17%, NO and NOx decreased by 58% and 57% respectively, and SO 2 decreased by 90%. For wood briquettes, emissions for CO decreased by 27%, NO and NOx decreased by 66%, and SO2 levels decreased by 97%. General trends in

  6. Experimental study on temperature distribution of membrane water wall in an ultra-supercritical pressure once-through boiler burning zhundong coal

    Science.gov (United States)

    He, Honghao; Li, Wenjun; Zeng, Jun; Xie, Guohong; Peng, Min; Duan, Xuenong

    2017-05-01

    Taking an ultra-supercritical pressure once-through boiler as an example, the temperature distribution of the lower membrane water wall is investigated experimentally, the conclusion reveals that increasing the proportion of Zhundong coal can effectively reduce the district heat load, which benefits the temperature uniformity in the lower membrane water wall. When the boiler being operated at middle load, the temperature deviation in lower membrane water wall increase simultaneously, one of the reasons is that the restriction orifice could not adjust the flow rate of working fluid as expected. By adjusting boiler performance, the temperature uniformity of lower membrane water wall can be improved to a certain degree.

  7. Shaft type lifting the coal consumption of boiler automatic metering counting device%轴式弧拉锅煤耗自动计量装置

    Institute of Scientific and Technical Information of China (English)

    朱炜淋

    2016-01-01

    This paper analyzes the existing problems of in use coal-fired industrial boilers for in recent years the country to implement energy-saving emission reduction work, and coal-fired industrial boiler energy-saving emission reduction transformation given investment and financing support measures, to improve the efficiency of coal-fired industrial boilers, and reduce pollutant emissions.%对近年来国家实施节能减排工作,对在用燃煤工业锅炉存在的问题进行分析。对燃煤工业锅炉节能减排改造给以投融资扶持等措施,以提高燃煤工业锅炉效率,减少污染物排放。

  8. Evaluation of hot corrosion behaviour of HVOF sprayed Ni-5Al and NiCrAl coatings in coal fired boiler environment

    Energy Technology Data Exchange (ETDEWEB)

    Mahesh, R.A.; Jayaganthan, R.; Prakash, S. [VA Tech EWF Pvt Ltd., Prithla (India)

    2010-08-15

    Hot corrosion was recognised as a serious problem in connection with the degradation of fireside boiler tubes in coal fired steam generating plants. It is one of the most deleterious forms of surface degradation which can lead to the loss of mechanical strength and catastrophic failure of structural and engineering components. In the present investigation, an attempt has been made to evaluate the hot corrosion behaviour of high velocity oxyfuel (HVOF) sprayed Ni-5Al and NiCrAl coatings on iron based superalloy in an actual coal fired boiler environment. The coated specimens were hung in the low temperature superheater zone (about 700{sup o}C) of a coal fired boiler. The studies were carried out for 10 cycles each cycle consisting of exposing the coated specimens for 100 h followed by 1 h cooling to ambient conditions. NiCrAl coated specimen provided better resistance to hot corrosion than Ni-5Al coated specimen in the given environment.

  9. A NOVEL SENSOR AND MEASUREMENT SYSTEM FOR FIRESIDE CORROSION MONITORING IN COAL-FIRED BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    Heng Ban; Zuoping Li

    2003-03-01

    Fireside corrosion in coal-fired power plants is a major obstacle to increase the overall efficiency for power producers. The increased use of opportunity fuels and low emission combustion modes have aggravated the corrosion on boiler tube walls in power plants. Corrosion-induced equipment failure could lead to catastrophic damage and inflict significant loss of production and cost for repair. Monitoring fireside corrosion in a reliable and timely manner can provide significant benefits to the plant operation. Current corrosion inspection and measurement are typically performed during scheduled maintenance outages, which is often after the damage is done. In the past, there have been many attempts to develop real time continuous corrosion monitoring technologies. However, there is still no short-term, online corrosion monitoring system commercially available for fireside corrosion to date due to the extremely harsh combustion environment. This report describes the results of a laboratory feasibility study on the development effort of a novel sensor for on-line fireside corrosion monitoring. A novel sensor principle and thin-film technologies were employed in the corrosion sensor design and fabrication. The sensor and the measurement system were experimentally studied using laboratory muffle furnaces. The results indicated that an accurate measure of corrosion rate could be made with high sensitivity using the new sensor. The investigation proved the feasibility of the concept and demonstrated the sensor design, sensor fabrication, and measurement instrumentation at the laboratory scale. An uncertainty analysis of the measurement system was also performed to provide a basis for further improvement of the system for future pilot or full scale testing.

  10. Suppression of fine ash formation in pulverized coal flames. Final technical report, September 30, 1992--January 31, 1996

    Energy Technology Data Exchange (ETDEWEB)

    Kramlich, J.C.; Chenevert, B.; Park, Jungsung; Hoffman, D.A.; Butcher, E.K.

    1996-07-19

    Coal ash, and particularly fine fly ash, remain one of the principal practical and environmental problems in coal-based power generation. In particular, submicron aerosols are identified with direct inhalation risk. Submicron ash is thought to arise from mineral vaporization during char combustion, followed by nucleation, condensation and coagulation to yield an aerosol. While aerosols are predominantly made out of volatile alkali minerals, they also can include refractory oxides that are chemically reduced to more volatile forms within the char particle and vaporized. Most of the ash of size greater than 1 {mu}m is generated by agglomeration of mineral as the char particle bums out. These two principal mechanisms are thought to account for most of the ash generated in coal combustion. Previous research has shown that various forms of coal treatment can influence the yields of fine ash from combustion. The research reported here investigates various forms of treatment, including physical coal cleaning, aerodynamic sizing, degree of grinding, and combinations of these on both aerosol yields and on yields of fine residual ash (1-4 {mu}m). The work also includes results from the combustion of artificial chars that include individual mineral elements. This research shows that these various forms of coal treatment can significantly change ash characteristics. While none of the treatments affected the bulk of the residual ash size distribution significantly, the yield of the ash aerosol mode (d<0.5 {mu}m) and fine residual ash mode (1-4 {mu}m) are changed by the treatments.

  11. An improvement method of pulverized coal caking problem and its application%一种有效改善煤粉结块问题的方法及其应用

    Institute of Scientific and Technical Information of China (English)

    汪林杰; 贾明生

    2013-01-01

    In accordance with the common phenomenon of coal caking in pulverized coal bunker, analyzed the factors of the factors of pulverized coal caking and put forward an effective solution to the problem of coal caking. In combination with the practical problem encountered in engineering practice, double - layer bunker made by ourselves can preheat the inside of the bunker and preserve the heat of it by means of roots blower , thus solving the problem of coal caking successfully.%针对煤粉仓普遍存在的结块搭桥的现象,分析了造成煤粉结块的主要因素,提出了一种有效改善煤粉结块问题的方法.结合工程实践中遇到的实际问题,自制研究了双层罐结构,并充分利用罗茨风机排气对双层罐内筒进行预热和保温,成功解决了粉仓结块的问题.

  12. A Novel Low-Temperature Fiffusion Aluminide Coating for Ultrasupercritical Coal-Fried Boiler Applications

    Energy Technology Data Exchange (ETDEWEB)

    Zhang, Ying

    2009-12-31

    An ultrasupercritical (USC) boiler with higher steam temperature and pressure is expected to increase the efficiency of the coal-fired power plant and also decrease emissions of air pollutants. Ferritic/martensitic alloys have been developed with good creep strength for the key components in coal-fired USC plants. However, they typically suffer excessive steam-side oxidation, which contributes to one of main degradation mechanisms along with the fire-side corrosion in coal-fired boilers. As the steam temperature further increases in USC boilers, oxidation of the tube internals becomes an increasing concern, and protective coatings such as aluminide-based diffusion coatings need to be considered. However, conventional aluminizing processes via pack cementation or chemical vapor deposition are typically carried out at elevated temperatures (1000-1150 C). Thermochemical treatment of ferritic/martensitic alloys at such high temperatures could severely degrade their mechanical properties, particularly the alloy's creep resistance. The research focus of this project was to develop an aluminide coating with good oxidation resistance at temperatures {le} 700 C so that the coating processing would not detrimentally alter the creep performance of the ferritic/martensitic alloys. Nevertheless, when the aluminizing temperature is lowered, brittle Al-rich intermetallic phases, such as Fe{sub 2}Al{sub 5} and FeAl{sub 3}, tend to form in the coating, which may reduce the resistance to fatigue cracking. Al-containing binary masteralloys were selected based on thermodynamic calculations to reduce the Al activity in the pack cementation process and thus to prevent the formation of brittle Al-rich intermetallic phases. Thermodynamic computations were carried out using commercial software HSC 5.0 for a series of packs containing various Cr-Al binary masteralloys. The calculation results indicate that the equilibrium partial pressures of Al halides at 700 C were a function of Al

  13. 航天炉粉煤贮罐过滤器堵煤原因分析及对策%Analysis of Causes for Coal Blocking in Filter of Pulverized Coal Storage Bunker of Hangtian Gasifier and Countermeasures

    Institute of Scientific and Technical Information of China (English)

    童维风; 郭兴建; 黄保才

    2012-01-01

    在航天炉从试车投产至稳定运行期间,多次出现粉煤贮罐过滤器锥部堵煤现象.经过逐一排查分析,发现是由于氮气吹扫管线风量较大、防雨罩结构不合理、贮罐内外温差较大导致粉煤贮罐过滤器锥部的堵煤.采取了有效的预防和整改措施后,解决了堵煤问题,保证了煤粉加压输送系统的长周期稳定运行.%In the period of the Hangtian gasifier from test run and commissioning up to stable running, coal blocks up the cone part of the filter in the bunker several times. After examination and analysis one by one it is found that the volume of nitrogen gas sweeping the pipeline is too large, the structure of the rain-proof cover is irrational, and the temperature difference between the inside and outside of the bunker is great, thus leading to coal blocking in the cone part of the filter in the bunker. Efficient prevention and rectification and reform measures are taken, the blocking is eliminated, thus guaranteeing the stable an long period operation of the pulverized coal conveyer.

  14. ADVANCED FLUE GAS CONDITIONING AS A RETROFIT UPGRADE TO ENHANCE PM COLLECTION FROM COAL-FIRED ELECTRIC UTILITY BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    Kenneth E. Baldrey

    2003-01-01

    The U.S. Department of Energy and ADA Environmental Solutions are engaged in a project to develop commercial flue gas conditioning additives. The objective is to develop conditioning agents that can help improve particulate control performance of smaller or under-sized electrostatic precipitators on utility coal-fired boilers. The new chemicals will be used to control both the electrical resistivity and the adhesion or cohesivity of the fly ash. There is a need to provide cost-effective and safer alternatives to traditional flue gas conditioning with SO{sub 3} and ammonia. During this reporting quarter, installation of a liquid flue gas conditioning system was completed at the American Electric Power Conesville Plant, Unit 3. This plant fires a bituminous coal and has opacity and particulate emissions performance issues related to fly ash re-entrainment. Two cohesivity-specific additive formulations, ADA-44C and ADA-51, will be evaluated. In addition, ammonia conditioning will also be compared.

  15. ADVANCED FLUE GAS CONDITIONING AS A RETROFIT UPGRADE TO ENHANCE PM COLLECTION FROM COAL-FIRED ELECTRIC UTILITY BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    C. Jean Bustard; Kenneth E. Baldrey; Richard Schlager

    2000-04-01

    The U.S. Department of Energy and ADA Environmental Solutions has begun a project to develop commercial flue gas conditioning additives. The objective is to develop conditioning agents that can help improve particulate control performance of smaller or under-sized electrostatic precipitators on utility coal-fired boilers. The new chemicals will be used to control both the electrical resistivity and the adhesion or cohesivity of the flyash. There is a need to provide cost-effective and safer alternatives to traditional flue gas conditioning with SO{sub 3} and ammonia. Preliminary testing has identified a class of common deliquescent salts that effectively control flyash resistivity on a variety of coals. A method to evaluate cohesive properties of flyash in the laboratory has been selected and construction of an electrostatic tensiometer test fixture is underway. Preliminary selection of a variety of chemicals that will be screened for effect on flyash cohesion has been completed.

  16. Computational intelligence approach for NO{sub x} emissions minimization in a coal-fired utility boiler

    Energy Technology Data Exchange (ETDEWEB)

    Zhou Hao, E-mail: zhouhao@cmee.zju.edu.c [State Key Laboratory of Clean Energy Utilization, Zhejiang University, Hangzhou 310027 (China); Zheng Ligang; Cen Kefa [State Key Laboratory of Clean Energy Utilization, Zhejiang University, Hangzhou 310027 (China)

    2010-03-15

    The current work presented a computational intelligence approach used for minimizing NO{sub x} emissions in a 300 MW dual-furnaces coal-fired utility boiler. The fundamental idea behind this work included NO{sub x} emissions characteristics modeling and NO{sub x} emissions optimization. First, an objective function aiming at estimating NO{sub x} emissions characteristics from nineteen operating parameters of the studied boiler was represented by a support vector regression (SVR) model. Second, four levels of primary air velocities (PA) and six levels of secondary air velocities (SA) were regulated by using particle swarm optimization (PSO) so as to achieve low NO{sub x} emissions combustion. To reduce the time demanding, a more flexible stopping condition was used to improve the computational efficiency without the loss of the quality of the optimization results. The results showed that the proposed approach provided an effective way to reduce NO{sub x} emissions from 399.7 ppm to 269.3 ppm, which was much better than a genetic algorithm (GA) based method and was slightly better than an ant colony optimization (ACO) based approach reported in the earlier work. The main advantage of PSO was that the computational cost, typical of less than 25 s under a PC system, is much less than those required for ACO. This meant the proposed approach would be more applicable to online and real-time applications for NO{sub x} emissions minimization in actual power plant boilers.

  17. Computational intelligence approach for NO{sub x} emissions minimization in a coal-fired utility boiler

    Energy Technology Data Exchange (ETDEWEB)

    Zhou, Hao; Zheng, Ligang; Cen, Kefa [State Key Laboratory of Clean Energy Utilization, Zhejiang University, Hangzhou 310027 (China)

    2010-03-15

    The current work presented a computational intelligence approach used for minimizing NO{sub x} emissions in a 300 MW dual-furnaces coal-fired utility boiler. The fundamental idea behind this work included NO{sub x} emissions characteristics modeling and NO{sub x} emissions optimization. First, an objective function aiming at estimating NO{sub x} emissions characteristics from nineteen operating parameters of the studied boiler was represented by a support vector regression (SVR) model. Second, four levels of primary air velocities (PA) and six levels of secondary air velocities (SA) were regulated by using particle swarm optimization (PSO) so as to achieve low NO{sub x} emissions combustion. To reduce the time demanding, a more flexible stopping condition was used to improve the computational efficiency without the loss of the quality of the optimization results. The results showed that the proposed approach provided an effective way to reduce NO{sub x} emissions from 399.7 ppm to 269.3 ppm, which was much better than a genetic algorithm (GA) based method and was slightly better than an ant colony optimization (ACO) based approach reported in the earlier work. The main advantage of PSO was that the computational cost, typical of less than 25 s under a PC system, is much less than those required for ACO. This meant the proposed approach would be more applicable to online and real-time applications for NO{sub x} emissions minimization in actual power plant boilers. (author)

  18. Ash liberation from included minerals during combustion of pulverized coal: the relationship with char structure and burnout

    Energy Technology Data Exchange (ETDEWEB)

    Wu, H.; Wall, T.; Liu, G.; Bryant, G. [University of Newcastle, Callaghan, NSW (Australia). CRC for Black Coal Utilization and Dept. of Chemical Engineering

    1999-12-01

    In this study, the float fraction ({lt} specific gravity of 2.0) of a size cut (63-90 {mu}m) bituminous coal was combusted in a drop tube furnace (DTF) at a gas temperature of 1300{degree}C under an atmosphere of air, to investigate the ash liberation at five coal burnoff levels (35.5%, 54.3%, 70.1%, 87.1% and 95.6%). The data indicated that char structure determines the ash liberation at different burnoff levels. Fragmentation of porous char was found to be the determinative mechanism for formation of fine ash during the early and middle stages of char combustion, while coalescence of included mineral matter determines the coarse ash formed in the later stages of combustion. The investigation confirmed that the char morphology and structure play a key role in determining char fragmentation, char burnout history, and the ash liberation during combustion. 35 refs., 5 figs., 2 tabs.

  19. Influence of Environmentally Friendly and High-Efficiency Composite Additives on Pulverized Coal Combustion in Cement Industry

    OpenAIRE

    2016-01-01

    4 kinds of chemical reagents and 3 kinds of industrial wastes were selected as burning additives for 2 kinds of coals in cement industry. The work focused on the replacement of partial chemical reagents by industrial wastes, which not only reduced the cost and took full advantage of industrial wastes, but also guaranteed the high combustion efficiency and removed the NOX and SO2 simultaneously. The experiments were carried out in DTF. The combustion residues were analyzed by SEM and XRD. The ...

  20. SAMPLING, ANALYSIS, AND PROPERTIES OF PRIMARY PM-2.5: APPLICATION TO COAL-FIRED UTILITY BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    Allen L. Robinson; Spyros N. Pandis; Eric Lipsky; Charles Stainer; Natalie Anderson; Satoshi Takahama; Sarah Rees

    2003-02-01

    A dilution sampler was used to examine the effects of dilution ratio and residence time on the particulate emissions from a pilot-scale pulverized coal combustor. Measurements include the particle size distribution from 0.003 to 2.5 {micro}m, PM{sub 2.5} mass emission rate and PM2.5 composition (OC/EC, major ions, and elemental). Hot filter samples were also collected simultaneously in order to compare the dilution sampler measurement with standard stack sampling methodologies such as EPA Method 5. Measurements were made both before and after the bag-house, the particle control device used on the coal combustor. Measurements were made with three different coal types and a coal-biomass blend. The residence time and dilution ratio do not influence the PM{sub 2.5} mass emission rate, but have a significant effect on the size distribution and total number emissions. Measurements made before the bag-house showed increasing the residence time dramatically decreases the total particle number concentration, and shifts the particle mass to larger sizes. The effects of residence time can be explained quantitatively by the coagulation of the emitted particles. Measurements made after the bag-house were not affected by coagulation due to the lower concentration of particles. Nucleation of sulfuric acid vapor within the dilution was an important source of ultrafine particles. This nucleation is strongly a function of dilution ratio because of the competition between condensation and nucleation. At low dilution ratios condensation dominates and little nucleation is observed; increasing the dilution ratio promotes nucleation because of the corresponding decrease in available surface area per unit volume for condensation. No nucleation was observed after the bag house where conditions greatly favor nucleation over condensation; we suspect that the bag house removed the SO{sub 3} in the flue gas. Exhaust SO{sub 3} levels were not measured during these experiments. Dilution caused

  1. A FUEL-RICH PRECOMBUSTOR. FIELD EVALUATION OF LOW-EMISSION COAL BURNER TECHNOLOGY ON UTILITY BOILERS - VOLUME IV. ALTERNATE CON- CEPTS FOR SOX, NOX, AND PARTICULATE EMISSIONS CONTROL FROM

    Science.gov (United States)

    The report gives results a study of the use of precombustors for the simultaneous control of S02, NOx, and ash emissions from coal combustion. In Phase 1, exploratory testing was conducted on a small pilot scale--293 kW (million Btu/hr)-pulverized-coal-fired precombustor to ident...

  2. Influence of Environmentally Friendly and High-Efficiency Composite Additives on Pulverized Coal Combustion in Cement Industry

    Directory of Open Access Journals (Sweden)

    Zhiyong Wang

    2016-01-01

    Full Text Available 4 kinds of chemical reagents and 3 kinds of industrial wastes were selected as burning additives for 2 kinds of coals in cement industry. The work focused on the replacement of partial chemical reagents by industrial wastes, which not only reduced the cost and took full advantage of industrial wastes, but also guaranteed the high combustion efficiency and removed the NOX and SO2 simultaneously. The experiments were carried out in DTF. The combustion residues were analyzed by SEM and XRD. The results showed that the burnout rate was increased after adding the additives; meanwhile, the NOX and SO2 release concentration were reduced, but the degree of action varied for different additives and coals. The substitute of chemical reagents by industrial wastes was very effective; overall, the cold-rolled iron oxide worked better than others; the particles surface was tougher and the peaks of crystalline phase were lower than raw coal, which indicated that the additives played good roles in combustion process.

  3. Investigation on Collection Performances of Plasma Signal for Pulverized Particle Coal Flow in Different Optical Collection%不同收光方式下煤粉流的等离子体信号探测

    Institute of Scientific and Technical Information of China (English)

    陈世和; 陆继东; 钟子铭; 潘凤萍; 潘刚; 张曦; 姚顺春; 罗嘉; 李军

    2013-01-01

    In order to reduce the adverse impact of the inhomogeneous of pulverized coal components, different optical path systems were set up and used to research the collection performances of plasma of pulverized coal by laser-induced breakdown spectroscopy. The coal samples, Shenmuhun, was chosen for experiment. The detected count and stability of special lines of coal in different optical collection were investigated on the self-built two-phase particle flow experiment bench, which was used to produce stable pulverized coal stream. The analysis results show that in the steadily repeat measurements, the counts of the lines collected by backside are weaker because of the intermediate perforated mirror, while the stability of the lines collected by side are worse because of the position change of plasma along the laser beam, the spatial inhomogeneity of plasma and the blocking effect of pulverized coal.%针对煤粉流组分分布的不均匀性,研究不同收光方式对煤粉流的激光诱导等离子体的光谱信号收集效果的影响.选用电厂常用燃煤神木混为实验对象,利用自行搭建的气固两相流实验台架产生稳定煤粉流,对比同向收光方式和侧向收光方式下煤的特征谱线信号探测的强度和稳定性.研究结果表明,相同实验条件下,中间穿孔反射镜使同向收光方式下探测的光谱信号强度较弱,而等离子体信号源位置沿激光束轴线的变化、等离子体信号本身沿空间分布的不均匀性及煤粉流的阻挡作用使侧向收光方式下探测的光谱信号稳定性较弱.

  4. The use of mechanically activated micronized coal in thermal power engineering

    Directory of Open Access Journals (Sweden)

    Burdukov Anatoliy P.

    2016-01-01

    Full Text Available Coal is one of the main energy resources and development of new promising technologies on its basis is certainly topical. This article discusses the use of new technology of gas and fuel oil replacement by mechanically activated micronized coal in power engineering: ignition and stabilization of pulverized coal flame combustion, as well as gasification of micronized coal in the flow. The new technology coal combustion with two stages of grinding is suggested. Optimization of the scheme of two-stage combustion is calculated. The first experimental data on the combustion process are obtained. The first demonstration tests on gas and heavy oil replacement by micronized coal during boiler ignition were carried out in the real power boiler with the capacity of 320 tons of steam per hour.

  5. Coal-fired power plants and the causes of high temperature corrosion

    Energy Technology Data Exchange (ETDEWEB)

    Oakey, J.E.; Simms, N.J. [British Coal Corporation, Coal Technology Development Div., Cheltenham, Glos (United Kingdom); Tomkings, A.B. [ERA Technology Ltd., Leatherhead, Surrey (United Kingdom)

    1996-12-01

    The heat exchangers in all types of coal-fired power plant operate in aggressive, high temperature environments where high temperature corrosion can severely limit their service lives. The extent of this corrosion is governed by the combined effects of the operating conditions of the heat exchanger and the presence of corrosive species released from the coal during operation. This paper reviews the coal-related factors, such as ash deposition, which influence the operating environments of heat exchangers in three types of coal-fired power plant - conventional pulverized coal boilers, fluidized bed boilers and coal gasification systems. The effects on the performance of the materials used for these heat exchangers are then compared. (au) 35 refs.

  6. Mixing of a reburn fuel in a cold model of a front-wall coal-fired boiler

    Energy Technology Data Exchange (ETDEWEB)

    Verlaan, A.L.; Dugue, J.; Weber, R. [International Flame Research Foundation, IJmuiden (Netherlands)

    1998-12-31

    An experimental research program has been carried out in order to determine the optimum reburn injection methods for pulverised coal fired boilers. Funding of this program was provided by the IFRF Members and the European Union (JOULE II extension, Project nr. 1B). The study is specifically concerned with the optimisation of natural gas reburning in front wall, pulverised coal fired boilers. The technical objectives are: to provide guidelines for optimising the reburn natural gas injection methods; to generate a set of simple empirical equations describing the trajectory, penetration distance and mixing time scales for practical nozzles; and to provide detailed experimental data that can be used to validate mathematical modelling computations. Using Laser Doppler Velocimetry the velocity profiles in the model are measured. The mixing characterisation is performed using Laser Sheet Visualisation, which creates images showing particle density over a plane of measurement. From these images properties are calculated such as: average intensity, RMS-intensity, intermittency, dissipation, unmixedness and spatial correlation. With this data simple relations are derived, describing jet penetration and mixing. 18 refs., 16 figs., 10 tabs.

  7. FEASIBILITY ANALYSIS FOR INSTALLING A CIRCULATING FLUIDIZED BED BOILER FOR COFIRING MULTIPLE BIOFUELS AND OTHER WASTES WITH COAL AT PENN STATE UNIVERSITY

    Energy Technology Data Exchange (ETDEWEB)

    Bruce G. Miller; Sharon Falcone Miller; Robert Cooper; John Gaudlip; Matthew Lapinsky; Rhett McLaren; William Serencsits; Neil Raskin; Tom Steitz; Joseph J. Battista

    2003-03-26

    The Pennsylvania State University, utilizing funds furnished by the U.S. Department of Energy's Biomass Power Program, investigated the installation of a state-of-the-art circulating fluidized bed boiler at Penn State's University Park campus for cofiring multiple biofuels and other wastes with coal, and developing a test program to evaluate cofiring biofuels and coal-based feedstocks. The study was performed using a team that included personnel from Penn State's Energy Institute, Office of Physical Plant, and College of Agricultural Sciences; Foster Wheeler Energy Services, Inc.; Foster Wheeler Energy Corporation; Parsons Energy and Chemicals Group, Inc.; and Cofiring Alternatives. The activities included assessing potential feedstocks at the University Park campus and surrounding region with an emphasis on biomass materials, collecting and analyzing potential feedstocks, assessing agglomeration, deposition, and corrosion tendencies, identifying the optimum location for the boiler system through an internal site selection process, performing a three circulating fluidized bed (CFB) boiler design and a 15-year boiler plant transition plan, determining the costs associated with installing the boiler system, developing a preliminary test program, determining the associated costs for the test program, and exploring potential emissions credits when using the biomass CFB boiler.

  8. Monitoring the species of arsenic, chromium and nickel in milled coal, bottom ash and fly ash from a pulverized coal-fired power plant in western Canada.

    Science.gov (United States)

    Goodarzi, F; Huggins, F E

    2001-02-01

    The concentration of As, Cr and Ni and their speciation (As3+;5+, Cr3+;6+ and Ni0;2+) in milled coal, bottom ash and ash collected by electrostatic precipitator (ESP) from a coal fired-power plant in western Canada were determined using HGAAS, ICP-AES and XANES. The chemical fractionation of these elements was also determined by a sequential leaching procedure, using deionized water, NH4OAC and HCI as extracting agents. The leachate was analyzed by ICP-AES. Arsenic in the milled coal is mostly associated with organic matter, and 67% of this arsenic is removed by ammonium acetate. This element is totally removed from milled coal after extraction with HCI. Arsenic occurs in both the As3+ and the As5+ oxidation states in the milled coal, while virtually all (>90%) of the arsenic in bottom ash and fly ash appears to be in the less toxic arsenate (As5+) form. Both Ni and Cr in the milled coal are extracted by HCI, indicating that water can mobilize Ni and Cr in an acidic environment. The chromium is leached by water from fly ash as a result of the high pH of the water, which is induced during the leaching. Ammonium acetate removes Ni from bottom ash through an ion exchange process. Chromium in milled coal is present entirely as Cr3+, which is an essential human trace nutrient. The Cr speciation in bottom ash is a more accentuated version of the milled coal and consists mostly of the Cr3+ species. Chromium in fly ash is mostly Cr3+, with significant contamination by stainless-steel from the installation itself.

  9. Modeling and full-scale tests of vortex plasma-fuel systems for igniting high-ash power plant coal

    Science.gov (United States)

    Messerle, V. E.; Ustimenko, A. B.; Karpenko, Yu. E.; Chernetskiy, M. Yu.; Dekterev, A. A.; Filimonov, S. A.

    2015-06-01

    The processes of supplying pulverized-coal fuel into a boiler equipped with plasma-fuel systems and its combustion in the furnace of this boiler are investigated. The results obtained from 3D modeling of conventional coal combustion processes and its firing with plasma-assisted activation of combustion in the furnace space are presented. The plasma-fuel system with air mixture supplied through a scroll is numerically investigated. The dependence of the swirled air mixture flow trajectory in the vortex plasma-fuel system on the scroll rotation angle is revealed, and the optimal rotation angle at which stable plasma-assisted ignition of pulverized coal flame is achieved is determined.

  10. Co-combustion of pulverized coal and solid recovered fuel in an entrained flow reactor- General combustion and ash behavior

    DEFF Research Database (Denmark)

    Wu, Hao; Glarborg, Peter; Frandsen, Flemming

    2011-01-01

    .9 wt.%, 14.8 wt.% and 25 wt.%, respectively. The effect of additives was evaluated by maintaining the share of secondary fuel (mixture of SRF and additive) at 14.8 wt.%. The experimental results showed that the fuel burnout, NO and SO2 emission in co-combustion of coal and SRF were decreased...... with increasing share of SRF. The majority of the additives inhibited the burnout, except for NaCl which seemed to have a promoting effect. The impact of additives on NO emission was mostly insignificant, except for ammonium sulphate which greatly reduced the NO emission. For SO2 emission, it was found that all...

  11. 400 t/h-50410A型燃油炉改燃煤炉可行性分析%Feasibility Analysis of Converting 50410A Type 410 t/h Oil-fired Boiler to Coal-fired Boiler

    Institute of Scientific and Technical Information of China (English)

    张明

    2001-01-01

    通过对400 t/h-50410A型锅炉本体、外围设施容量、选型及布置、改造费用与燃料差价等方面的技术分析及经济比较,认为将其改造为燃煤炉是可行的;同时对煤种结焦特性、炉膛热负荷强度、尾部气流冲刷、燃油与燃煤的SO2排放等方面进行分析,并提出改造后应注意的问题及改进措施。%Through the technical analyses of boiler proper capacities type selection and layout of peripheral facilities as well as the economic comparison of retrofitting cost and price differentials between coal and oil it is considered that to convert the existing boiler to coal-fired is feasible. At the same time the slagging property of coal thermal intensity of furnace gasflow swept of boiler tail SO2 emission of oil-firing and coal-firing etc. aspects are analyzed and the problems needing attention and improving measures after retrofitting are put forward.

  12. Ultra-Supercritical Pressure CFB Boiler Conceptual Design Study

    Energy Technology Data Exchange (ETDEWEB)

    Zhen Fan; Steve Goidich; Archie Robertson; Song Wu

    2006-06-30

    Electric utility interest in supercritical pressure steam cycles has revived in the United States after waning in the 1980s. Since supercritical cycles yield higher plant efficiencies than subcritical plants along with a proportional reduction in traditional stack gas pollutants and CO{sub 2} release rates, the interest is to pursue even more advanced steam conditions. The advantages of supercritical (SC) and ultra supercritical (USC) pressure steam conditions have been demonstrated in the high gas temperature, high heat flux environment of large pulverized coal-fired (PC) boilers. Interest in circulating fluidized bed (CFB) combustion, as an alternative to PC combustion, has been steadily increasing. Although CFB boilers as large as 300 MWe are now in operation, they are drum type, subcritical pressure units. With their sizes being much smaller than and their combustion temperatures much lower than those of PC boilers (300 MWe versus 1,000 MWe and 1600 F versus 3500 F), a conceptual design study was conducted herein to investigate the technical feasibility and economics of USC CFB boilers. The conceptual study was conducted at 400 MWe and 800 MWe nominal plant sizes with high sulfur Illinois No. 6 coal used as the fuel. The USC CFB plants had higher heating value efficiencies of 40.6 and 41.3 percent respectively and their CFB boilers, which reflect conventional design practices, can be built without the need for an R&D effort. Assuming construction at a generic Ohio River Valley site with union labor, total plant costs in January 2006 dollars were estimated to be $1,551/kW and $1,244/kW with costs of electricity of $52.21/MWhr and $44.08/MWhr, respectively. Based on the above, this study has shown that large USC CFB boilers are feasible and that they can operate with performance and costs that are competitive with comparable USC PC boilers.

  13. Ensuring slagging-free operation of a boiler equipped with hammer mills in firing brown coal with low-melting ash

    Science.gov (United States)

    Arkhipov, A. M.; Dorogoi, G. A.

    2011-04-01

    The possibility of ensuring slagging-free operation of heating surfaces in firing Pereyaslov brown coal is considered taking the PK-38 boiler at the Krasnoyarsk GRES-2 district power station as an example. Retrofitting of burners and nozzles and setting up of a recirculation-vortex flame are recommended.

  14. Innovative clean coal technology (ICCT): Demonstration of selective catalytic reduction (SCR) technology for the control of nitrogen oxide (NO{sub x}) emissions from high-sulfur coal-fired boilers. Quarterly report No. 3, January--March 1991

    Energy Technology Data Exchange (ETDEWEB)

    1991-07-01

    The objective of this project is to demonstrate and evaluate commercially available Selective Catalytic Reduction (SCR) catalysts from US, Japanese and European catalyst suppliers on a high-sulfur US coal-fired boiler. SCR is a post-combustion nitrogen oxide (NOx) control technology that involves injecting ammonia into the flue gas generated from coal combustion in an electric utility boiler. The flue gas containing ammonia is then passed through a reactor that contains a specialized catalyst. In the presence of the catalyst, the ammonia reacts with NOx to convert it to nitrogen and water vapor.

  15. Innovative clean coal technology (ICCT): Demonstration of selective catalytic reduction (SCR) technology for the control of nitrogen oxide (NO sub x ) emissions from high-sulfur coal-fired boilers

    Energy Technology Data Exchange (ETDEWEB)

    1991-07-01

    The objective of this project is to demonstrate and evaluate commercially available Selective Catalytic Reduction (SCR) catalysts from US, Japanese and European catalyst suppliers on a high-sulfur US coal-fired boiler. SCR is a post-combustion nitrogen oxide (NOx) control technology that involves injecting ammonia into the flue gas generated from coal combustion in an electric utility boiler. The flue gas containing ammonia is then passed through a reactor that contains a specialized catalyst. In the presence of the catalyst, the ammonia reacts with NOx to convert it to nitrogen and water vapor.

  16. Innovative Clean Coal Technology (ICCT). Demonstration of Selective Catalytic Reduction (SCR) technology for the control of Nitrogen Oxide (NO{sub x}) emissions from high-sulfur coal-fired boilers. Technical progress report, third and fourth quarters 1995

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1996-05-01

    The objective of this project is to demonstrate and evaluate commercially available Selective Catalytic Reduction (SCR) catalysts from U.S., Japanese, and European catalyst suppliers on a high-sulfur U.S. coal-fired boiler. SCR is a post-combustion nitrogen oxide (NO{sub x}) control technology that involves injecting ammonia into the flue gas generated from coal combustion in an electric utility boiler. The flue gas containing ammonia is then passed through a reactor that contains a specialized catalyst. In the presence of the catalyst, the ammonia reacts with NO{sub x} to convert it to nitrogen and water vapor.

  17. Innovative Clean Coal Technology (ICCT): Demonstration of Selective Catalytic Reduction (SCR) technology for the control of nitrogen oxide (NO sub x ) emissions from high-sulfur coal-fired boilers

    Energy Technology Data Exchange (ETDEWEB)

    1991-02-01

    The objective of this project is to demonstrate and evaluate commercially available Selective Catalytic Reduction (SCR) catalysts from US, Japanese and European catalyst suppliers on a high-sulfur US coal-fired boiler. SCR is a post-combustion nitrogen oxide NO{sub x} control technology that involves injecting ammonia into the flue gas generated from coal combustion in an electric utility boiler. The flue gas containing ammonia is then passed through a reactor that contains a specialized catalyst. In the presence of the catalyst, the ammonia reacts with NO{sub x} to convert it to nitrogen and water vapor.

  18. Innovative Clean Coal Technology (ICCT): Demonstration of Selective Catalytic Reduction (SCR) technology for the control of nitrogen oxide (NO{sub x}) emissions from high-sulfur coal-fired boilers. Quarterly report No. 2, October--December 1990

    Energy Technology Data Exchange (ETDEWEB)

    1991-02-01

    The objective of this project is to demonstrate and evaluate commercially available Selective Catalytic Reduction (SCR) catalysts from US, Japanese and European catalyst suppliers on a high-sulfur US coal-fired boiler. SCR is a post-combustion nitrogen oxide NO{sub x} control technology that involves injecting ammonia into the flue gas generated from coal combustion in an electric utility boiler. The flue gas containing ammonia is then passed through a reactor that contains a specialized catalyst. In the presence of the catalyst, the ammonia reacts with NO{sub x} to convert it to nitrogen and water vapor.

  19. Experimental Study on NOx Reduction in a Coal-fired Boiler by Reburning Biomass Syngas with Tar%含焦油生物质气再燃还原燃煤锅炉NOx的试验研究

    Institute of Scientific and Technical Information of China (English)

    殷仁豪; 罗永浩; 刘春元; 张睿智; 曹阳

    2012-01-01

    A test rig, consisting of a 10 kW updraft biomass gasifier and a 20 kW pulverized-coal drop tube furnace, was established to investigate the technology of NOx reduction in a coal-fired boiler by reburning biomass syngas with tar under different reburning conditions. Results show that the tar produced in gasification process will crack into hydrocarbon radicals with high heat value, which have a positive effect on NOx reduction. Higher efficiency of NO, reduction may be obtained at lower excess air coefficients and higher reburning temperatures, and in the experiment, the data may get above 80%. The application of bi omass syngas reburning technology may help to handle the tough problem of tar disposal, raise conversion rate of biomass energy, and simultaneously reduce NOx emission from coal-fired boilers.%搭建了10kW上吸式生物质气化炉和20kW煤粉沉降炉组成的生物质气化再燃试验系统,分析了不同再燃条件下含焦油生物质气再燃还原燃煤锅炉NOx的特性.结果表明:气化过程中产生的焦油在再燃过程中会裂解生成高热值的烃类气体,这些烃类气体还原NOx的效果明显;当过量空气系数较小、再燃温度较高时,NOx的还原效率较高,试验中最高还原效率超过80%;采用生物质气化再燃的方式既可以解决焦油难处理的问题,又可以提高生物质能量的转化效率,同时可高效降低燃煤锅炉NOx的排放量.

  20. A new technique to measure the amount of unburnt coal in the ashes of a coal fired boiler

    Energy Technology Data Exchange (ETDEWEB)

    Bramanti, M.; De Michele, G.; Saccenti, G.

    1987-02-01

    The method normally used to measure the amount of unburnt coal in the ashes of coal combustion is chemical analysis. This procedure gives us results of great precision but not in real time. Coal ashes without unburnt coal behave as a perfect dielectric material, while the unburnt coal has a notable value of conductivity. The present paper proposes a new method to measure in real time the amount of unburnt coal in the ashes. The technique proposed is founded on the determination of the reflection coefficient of an electromagnetic microwave propagating in a microstrip transmission system and reflected by the ashes under test. The new method of measurement is covered by an ENEL-CNR patent.

  1. 运行参数对粉煤流化床(PC-FB)燃烧效率的影响%The Effect of Operation Parameters on the Combustion Efficiency of a Pulverized-coal Fluidized Bed

    Institute of Scientific and Technical Information of China (English)

    陈鸿伟; 金保升; 徐益谦

    2001-01-01

    With the help of a pulverized-coal fluidized bed (PC-FB) test rig with 0.3 MW heat input test data were obtained of the PC-FB combustion efficiency under various operation parameters. A detailed discussion and study was conducted focusing on the mechanism of influence of these operation parameters on PC-FB combustion efficiency. The study results indicate that the combustion efficiency of the PC-FB can be as high as 98% - 99%, comparable with that of a pulverized-coal furnace. The authors also pointed out for the first time in the present study that under a certain set of conditions it is possible to realize a low-temperature high-efficiency combustion of the pulverized-coal. These conditions include, among others, a rational matching of the following items: combustion temperature, particle residence time, flame turbulence and in-furnace oxygen concentration and particle concentration%在一座0.3 MW热输入的PC-FBC试验台上进行了试验研究,获得了不同操作参数下PC-FB燃烧效率的试验数据,详细讨论了这些参数对PC-FB燃烧效率的影响规律。研究结果表明,粉煤流化床的燃烧效率最高达98%~99%,可与煤粉炉相媲美。本试验研究亦首次提出,只要燃烧温度、颗粒停留时间、火焰湍流度(3T)及炉内氧浓度、颗粒浓度(2C)合理匹配,就能够实现煤粉的低温高效燃烧。

  2. Investigations of operation problems at a 200 MWe PF boiler

    Directory of Open Access Journals (Sweden)

    Peta Sandile

    2015-09-01

    Full Text Available To minimize oxides of nitrogen (NOx emission, maximize boiler combustion efficiency, achieve safe and reliable burner combustion, it is crucial to master global boiler and at-the-burner control of fuel and air flows. Non-uniform pulverized fuel (PF and air flows to burners reduce flame stability and pose risk to boiler safety by risk of reverse flue gas and fuel flow into burners. This paper presents integrated techniques implemented at pilot ESKOM power plants for the determination of global boiler air/flue gas distribution, wind-box air distribution and measures for making uniform the flow being delivered to burners within a wind-box system. This is achieved by Process Flow Modelling, at-the-burner static pressure measurements and CFD characterization. Global boiler mass and energy balances combined with validated site measurements are used in an integrated approach to calculate the total (stoichiometric + excess air mass flow rate required to burn the coal quality being fired, determine the actual quantity of air that flows through the burners and the furnace ingress air. CFD analysis and use of at-the-burner static, total pressure and temperature measurements are utilized in a 2-pronged approach to determine root-causes for burner fires and to evaluate secondary air distribution between burners.

  3. Boiler conversions for biomass

    Energy Technology Data Exchange (ETDEWEB)

    Kinni, J. [Tampella Power Inc., Tampere (Finland)

    1996-12-31

    Boiler conversions from grate- and oil-fired boilers to bubbling fluidized bed combustion have been most common in pulp and paper industry. Water treatment sludge combustion, need for additional capacity and tightened emission limits have been the driving forces for the conversion. To accomplish a boiler conversion for biofuel, the lower part of the boiler is replaced with a fluidized bed bottom and new fuel, ash and air systems are added. The Imatran Voima Rauhalahti pulverized-peat-fired boiler was converted to bubbling fluidized bed firing in 1993. In the conversion the boiler capacity was increased by 10 % to 295 MWth and NO{sub x} emissions dropped. In the Kymmene Kuusankoski boiler, the reason for conversion was the combustion of high chlorine content biosludge. The emissions have been under general European limits. During the next years, the emission limits will tighten and the boilers will be designed for most complete combustion and compounds, which can be removed from flue gases, will be taken care of after the boiler. (orig.) 3 refs.

  4. Co-combustion of pulverized coal and solid recovered fuel in an entrained flow reactor - General combustion and ash behaviour

    Energy Technology Data Exchange (ETDEWEB)

    Hao Wu; Peter Glarborg; Flemming Jappe Frandsen; Kim Dam-Johansen; Peter Arendt Jensen; Bo Sander [Technical University of Denmark, Lyngby (Denmark). Department of Chemical and Biochemical Engineering

    2011-05-15

    Co-combustion of a bituminous coal and a solid recovered fuel (SRF) was carried out in an entrained flow reactor, and the influence of additives such as NaCl, PVC, ammonium sulphate, and kaolinite was investigated. The experiments were carried out with SRF shares of 7.9 wt.%, 14.8 wt.% and 25 wt.%, respectively. The effect of additives was evaluated by maintaining the share of secondary fuel (mixture of SRF and additive) at 14.8 wt.%. The results showed that fuel burnout, NO and SO{sub 2} emission decreased with increasing share of SRF. The majority of the additives inhibited the burnout, except for NaCl which seemed to have a promoting effect. The impact of additives on NO emission was mostly insignificant, except for ammonium sulphate which greatly reduced NO emission. For SO{sub 2}, it was found that all of the additives increased the S-retention in ash. Analysis of the bulk composition of fly ash from different experiments indicated that the majority of S and Cl in the fuels were released to gas phase during combustion, whereas the K and Na in the fuels were mainly retained in ash in water insoluble form such as aluminosilicates or silicates. The addition of NaCl, PVC, and ammonium sulphate generally promoted the vaporization of Na and K, resulting in increased formation of water soluble alkalis such as alkali chlorides or sulphates. The vaporization degree of Na and K was found to be correlated during the experiments, suggesting an interaction between the vaporization of Na and K during combustion. By collecting deposits on an air-cooled probe, it was found that the ash deposition propensity in co-combustion decreased with increasing share of SRF. The addition of NaCl and PVC significantly increased the ash deposition propensity, whereas the addition of ammonium sulphate or kaolinite showed a slight reducing effect. 46 refs., 13 figs., 2 tabs.

  5. Optimize to pulverizing system control method for the Indonesian high moisture lignite coal%针对印尼高水分褐煤的制粉系统优化控制方法

    Institute of Scientific and Technical Information of China (English)

    程学安

    2012-01-01

      This paper introduces the main problem of the lignite pulverizing system of large power stations, the use of actual production experience in Indonesia, for high-moisture lignite explosive the drying capacity demand large, the optimal control method. Domestic medium-speed mill boilers fueled with high moisture lignite certain reference.%  该文介绍了现有燃用褐煤的大型电站的制粉系统出现的主要问题,并利用在印尼实际的生产经验,针对高水分褐煤易爆炸,干燥出力需求大等特点,提出了相应的优化控制方法。对国内中速磨锅炉燃用高水分褐煤有一定的借鉴作用。

  6. Theoretical Research of Coal Gasification Products Burning in Boilers at Tomsk Thermal Power Plant-3

    Directory of Open Access Journals (Sweden)

    Somov A.A.

    2015-01-01

    Full Text Available Mathematical modeling of primary fuel change into power gas in power generating boiler with productivity of steam 160 t\\h was done. Research of aggregate work on some power modes was completed. Characteristic curves of efficiency coefficient at different loads and ratio on power and natural gases burning were made. Practicability of power gas use as fuel was proved.

  7. Co-firing Coal and Straw in a 150 MWe Utility Boiler: Deposition Propensities

    DEFF Research Database (Denmark)

    Andersen, Karin Hedebo; Hansen, Peter Farkas Binderup; Wieck-Hansen, Kate;

    1996-01-01

    In order to meet a 20 % reduction in CO2 emissions, based on 1988 levels, by the year 2005, the Danish Government has committed the power companies in Denmark to burn 1.2 million tons of straw per year from the year 2000. A conventional pf-fired boiler at the Danish Power Company Midtkraft has be...

  8. Development of Cost Effective Oxy-Combustion Retrofitting for Coal-Fired Boilers

    Energy Technology Data Exchange (ETDEWEB)

    Hamid Farzan

    2010-12-31

    The overall objective of this project is to further develop the oxy-combustion technology for commercial retrofit in existing wall-fired and Cyclone boilers by 2012. To meet this goal, a research project was conducted that included pilot-scale testing and a full-scale engineering and economic analysis.

  9. [Engineering development of advanced coal-fired low-emission boiler systems]. Technical progress report, October--December 1995

    Energy Technology Data Exchange (ETDEWEB)

    Wesnor, J.D.; Bakke, E. [ABB Environmental Systems, Birmingham, AL (United States); Bender, D.J.; Kaminski, R.S. [Raytheon Engineers and Constructors, Inc., Philadelphia, PA (United States)

    1995-12-31

    The overall objective of the Project is the expedited commercialization of advanced coal-fired low-emisssion boiler systems. The primary objectives are: NO{sub x} emissions, lb/million Btu; SO{sub 2} emissions, lb/million Btu; particulate emissions, lb/million Btu; and net plant efficiency, not less than 42%. The secondary objectives are: improved ash disposability; reduced waste generation; and reduced air toxics emissions. Accomplishments to date are summarized for the following tasks: task 1, project planning and management; task 7, component development and optimization; task 8, preliminary POC test facility design; task 9, subsystem test design and plan; task 10, subsystem test unit construction; and task 11, subsystem test operation and evaluation.

  10. Least Square Fast Learning Network for modeling the combustion efficiency of a 300WM coal-fired boiler.

    Science.gov (United States)

    Li, Guoqiang; Niu, Peifeng; Wang, Huaibao; Liu, Yongchao

    2014-03-01

    This paper presents a novel artificial neural network with a very fast learning speed, all of whose weights and biases are determined by the twice Least Square method, so it is called Least Square Fast Learning Network (LSFLN). In addition, there is another difference from conventional neural networks, which is that the output neurons of LSFLN not only receive the information from the hidden layer neurons, but also receive the external information itself directly from the input neurons. In order to test the validity of LSFLN, it is applied to 6 classical regression applications, and also employed to build the functional relation between the combustion efficiency and operating parameters of a 300WM coal-fired boiler. Experimental results show that, compared with other methods, LSFLN with very less hidden neurons could achieve much better regression precision and generalization ability at a much faster learning speed.

  11. Study on solidification and stabilization technique by steam treatment of the coal ash from fluidized-bed combustion boilers; Ryudoso sekitanbai no joki shori ni yoru koka / anteika gijutsu ni kansuru kenkyu

    Energy Technology Data Exchange (ETDEWEB)

    Shibata, Y. [Kawasaki Heavy Industries Ltd., Kobe (Japan)

    1998-08-20

    In fluidized-bed coal combustion boiler supporting one end of boilers for power generation and process heating, coal ash comprised of the products of ash of coal and lime stone used for desulfurizer was used for raw material. The fluidized-bed combustion boiler really working at present is of normal pressure (AFBC) type due to bubbling or cycling system, and pressure type of the bubbling system (PFBC) due to high pressure of about 1.0 MPa is promoted development for a next generation type power generation. Then, by using the coal ash obtained from the AFBC boiler with different kind of coal, volume of boiler, and so on (AFBC ash) and the coal ash obtained from the PFBC boiler under actual proof operation, a study on properties of coal, lime stone and solids after steam treatment of mixture with water (kind/volume, strength and elution of hazard heavy metals of hydrates) were conducted to investigate to use for civil engineering materials such as road materials, filling back materials, and so forth. 16 refs., 13 figs., 2 tabs.

  12. Prediction of combustion behavior of coal blends in industrial scale boilers from laboratory scale data

    Energy Technology Data Exchange (ETDEWEB)

    Pisupati, S.V.; Scaroni, A.W. [Pennsylvania State Univ., University Park, PA (United States). Coal Utilization Lab.

    1997-12-31

    Thermal analytical techniques such as thermogravimetric analysis (TGA) have been used extensively in characterizing the thermal behavior of coals. Studies have shown that burning profiles are useful for evaluating laboratory scale combustion characteristics. Blending of coals is common in the utility industry to meet emission regulations and lower fuel costs. In this paper, it is shown that using burning profiles to predict carbon burnout of individual coals and blends in a practical combustor is appropriate. (orig.)

  13. 500 MW demonstration of advanced wall-fired combustion techniques for the reduction of nitrogen oxide emissions from coal-fired boilers

    Energy Technology Data Exchange (ETDEWEB)

    Sorge, J.N. [Southern Co. Services, Inc., Birmingham, AL (United States); Menzies, B. [Radian Corp., Austin, TX (United States); Smouse, S.M. [USDOE Pittsburgh Energy Technology Center, PA (United States); Stallings, J.W. [Electric Power Research Inst., Palo Alto, CA (United States)

    1995-09-01

    Technology project demonstrating advanced wall-fired combustion techniques for the reduction of nitrogen oxide NOx emissions from coal-fired boilers. The primary objective of the demonstration is to determine the long-term NOx reduction performance of advanced overfire air (AOFA), low NOx burners (LNB), and advanced digital control/optimization methodologies applied in a stepwise fashion to a 500 MW boiler. The focus of this paper is to report (1) on the installation of three on-line carbon-in-ash monitors and (2) the design and results to date from the advanced digital control/optimization phase of the project.

  14. Ash transformation in suspension fired boilers co-firing coal and straw

    DEFF Research Database (Denmark)

    Zheng, Yuanjing; Jensen, Peter Arendt; Jensen, Anker Degn

    Appendix C: Paper in Fuel 87 (2008) 3304-3312: A kinetic study of gaseous potassium capture by coal minerals in a high temperature fixed-bed reactor......Appendix C: Paper in Fuel 87 (2008) 3304-3312: A kinetic study of gaseous potassium capture by coal minerals in a high temperature fixed-bed reactor...

  15. 干法粉煤加压气化技术的开发现状和应用前景%Development Situation and Application Prospects of Pressure Dry Pulverized Coal Gasification Technology

    Institute of Scientific and Technical Information of China (English)

    门长贵

    2000-01-01

    干法粉煤加压气化是一种高效低污染的先进煤气化方法。本文简要介绍了干法粉煤加压气化的工艺原理、技术特点及开发现状,并指出了这种煤气化工艺技术在联合循环发电和煤化工等领域内的应用前景。%Pressure dry pulverized coal gasification is an advanced coal gasification technology for high efficiency and low pollution. This article mainly presents its processprinciple, technology characteristics and development situa-tion, as well as application prospects in the fields of IGCCand chemical industry.

  16. Influence of process parameters on coal combustion performance. Review, experiments and engineering modeling

    Energy Technology Data Exchange (ETDEWEB)

    Lans, R.P. van der

    1997-04-01

    The objective of this study is to improve the understanding of nitrogen oxide formation and carbon burnout during the combustion of pulverized coal, and to contribute to addressing the potential of chemical engineering models for the prediction of furnace temperatures, NO emissions and the amount of carbon in ash. To this purpose, the effect of coal quality on NO and burnout has been investigated experimentally, a radiation heat balance has been developed based on a simple chemical engineering methodology, and a mixing study has been conducted in order to describe the near burner macro mixing in terms of a reactor configuration. The influence of coal type and process conditions on NO formation and carbon burnout has been investigated experimentally in a 400 MW{sub e} corner fired boiler with over fire air, a 350 MW{sub e} opposed fired boiler, and in a 160 kW{sub t} pilot scale test rig. Three different coals were fired in each of the furnaces as part of the activities in group 3 of the European Union JOULE 2 Extension project `Atmospheric Pressure Combustion of Pulverized Coal and Coal Based Blends for Power Generation`. On the pilot scale test both single stage and air staged tests were performed. A simple, one-dimensional combustion and radiation heat transfer model has been developed for the furnace of full scale boilers. The model has been applied to the two boilers mentioned above, and is validated against measured temperatures and carbon in ash concentrations. A mixing study has been performed in order to initiate an investigation of the potential of chemical engineering models to predict NO from pulverized fuel burners. (EG) 11 refs.

  17. Demonstration of selective catalytic reduction (SCR) technology for the control of nitrogen oxide (NO sub x ) emissions from high-sulfur coal-fired boilers

    Energy Technology Data Exchange (ETDEWEB)

    1991-08-01

    The objective of this project is to demonstrate and evaluate commercially available Selective Catalytic Reduction (SCR) catalysts from US, Japanese and European catalyst suppliers on a high-sulfur US coal-fired boiler. SCR is a post-combustion nitrogen oxide (NOx) control technology that involves injecting ammonia into the flue gas generated from coal combustion in an electric utility boiler. The flue gas containing ammonia is then passed through a reactor that contains a specialized catalyst. In the presence of the catalyst, the ammonia reacts with NOx to convert it to nitrogen and water vapor, Although SCR is widely practiced in Japan and Europe, there are numerous technical uncertainties associated with applying SCR to US coals. These uncertainties include: (1) potential catalyst deactivation due to poisoning by trace metal species present in US coals that are not present in other fuel performance of the technology and effects on the balance-of-plant equipment in the presence of high amounts of SO{sub 2} and SO{sub 3}. (3) performance of a wide variety of SCR catalyst compositions, geometries and methods of manufacture under typical high-sulfur coal-fired utility operating conditions. These uncertainties will be explored by constructing a series of small-scale SCR reactors and simultaneously exposing different SCR catalysts to flue gas derived from the combustion of high sulfur US coal.

  18. Demonstration of selective catalytic reduction (SCR) technology for the control of nitrogen oxide (NO[sub x]) emissions from high-sulfur coal-fired boilers

    Energy Technology Data Exchange (ETDEWEB)

    1992-08-01

    The objective of this project is to demonstrate and evaluate commercially available Selective Catalytic Reduction (SCR) catalysts from US, Japanese and European catalyst suppliers on a high-sulfur US coal-fired boiler. SCR is a post-combustion nitrogen oxide (NO[sub x]) control technology that involves injecting ammonia into the flue gas generated from coal combustion in an electric utility boiler. The flue gas containing ammonia is then passed through a reactor that contains a specialized catalyst. In the presence of the catalyst, the ammonia reacts with NO[sub x] to convert it to nitrogen and water vapor. Although SCR is widely practiced in Japan and Europe, there are numerous technical uncertainties associated with applying SCR to US coals. These uncertainties include: (1) potential catalyst deactivation due to poisoning by trace metal species present in US coals that are not present in other fuels. (2) performance of the technology and effects on the balance-of-plant equipment in the presence of high amounts of SO[sub 2] and SO[sub 3]. (3) performance of a wide variety of SCR catalyst compositions, geometries and methods of manufacture under typical high-sulfur coal-fired utility operating conditions. These uncertainties will be explored by constructing a series of small-scale SCR reactors and simultaneously exposing different SCR catalysts to flue gas derived from the combustion of high sulfur U. S. coal.

  19. Erosion-corrosion of as-plasma-sprayed and laser-remelted NiCrAlY bond coats in working conditions of a coal-fired boiler

    Energy Technology Data Exchange (ETDEWEB)

    Sidhu, B.S.; Prakash, S. [College of Engineering & Technology, Bathinda (India). Dept. of Mechanical Engineering

    2008-01-15

    Ni-22Cr-10Al-1Y plasma spray coating has been formulated on boiler tube steels. namely, low-carbon steel ASTM SA210-Grade A1. 1Cr-0.5Mo steel ASTM SA213-T-11, and 2.25Cr-1Mo steel ASTM SA213-T-22. The coated steels also have been laser-remelted using a Nd:YAG laser. The degradation behavior of as-sprayed and laser-remelted coatings have been evaluated in actual conditions in a coal-fired boiler for 1,000 h at 755{sup o}C. The laser remelting has been found to be effective to increase the degradation resistance of plasma-sprayed boiler steels. ASTM SA213-T-22-coated and laser-remelted steel has proved to be most effective in resistance to degrading species.

  20. Aspects chimiques de la combustion du charbon pulvérisé. Première partie Chemical Aspects of the Combustion of Pulverized Coal. Part One

    Directory of Open Access Journals (Sweden)

    De Soete G. G.

    2006-11-01

    deux mécanismes totalement différents, par exemple entre le mécanisme d'ignition homogène et le mécanisme d'ignition hétérogène du charbon, avec des conséquences pratiques pour la stabilisation de la flamme industrielle ; autre exemple : la compétition entre les divers mécanismes homogènes de formation d'oxydes d'azote et les mécanismes hétérogènes de leur réduction sur des particules solides de coke, de suie et de cendre. Avec ces idées présentes comme un leitmotiv implicite, on passe en revue les grandes étapes de la flamme industrielle de charbon pulvérisé : la dévolatilisation rapide avec la formation progressive de volatils gazeux, de goudrons et de coke ; la transformation partielle des produits gazeux et liquides de pyrolyse en suies ainsi que leur oxydation en phase gazeuse ; la combustion hétérogène du coke ; l'ignition du charbon et sa dépendance par rapport à des processus critiques homogènes et (ou hétérogènes. Comme exemple typique d'un épiphénomènechimique, on suit la transformation des espèces azotées en NO et en N2, qui se greffe en contrepoint et à chaque pas sur tes différents thèmes successifs de cette symphonie de l'oxydation du charbon. En de nombreux points de cette évolution du charbon à travers la flamme, les connaissances de la chimie de com-bustion en phase gazeuse constituent un instrument utile d'interprétation (par exemple : pour l'oxydation des volatils, pour la discussion des modalités d'ignition. II n'en reste pas moins vrai que la plupart des problèmes chimiques hétérogènes sont bien spécifiques de la flamme de charbon ; leur traitement est rendu ardu à cause de la complexité, évolutive au cours de la combustion, du combustible solide lui-même. It is not easy to obtain a full picture of the multiple chemical phenomena which occur inside a pulverized coal flame. This bibliographie review attempts to give more than just a juxtaposition of data from the recent literature and risks making

  1. ADVANCED FLUE GAS CONDITIONING AS A RETROFIT UPGRADE TO ENHANCE PM COLLECTION FROM COAL-FIRED ELECTRIC UTILITY BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    Kenneth E. Baldrey

    2002-05-01

    The U.S. Department of Energy and ADA Environmental Solutions are engaged in a project to develop commercial flue gas conditioning additives. The objective is to develop conditioning agents that can help improve particulate control performance of smaller or under-sized electrostatic precipitators on utility coal-fired boilers. The new chemicals will be used to control both the electrical resistivity and the adhesion or cohesivity of the fly ash. There is a need to provide cost-effective and safer alternatives to traditional flue gas conditioning with SO{sub 3} and ammonia. During this reporting quarter, performance testing of flue gas conditioning was underway at the PacifiCorp Jim Bridger Power Plant. The product tested, ADA-43, was a combination resistivity modifier with cohesivity polymers. This represents the first long-term full-scale testing of this class of products. Modifications to the flue gas conditioning system at Jim Bridger, including development of alternate injection lances, was also undertaken to improve chemical spray distribution and to avoid spray deposition to duct interior surfaces. Also in this quarter, a firm commitment was received for another long-term test of the cohesivity additives. This plant fires a bituminous coal and has opacity and particulate emissions performance issues related to fly ash re-entrainment. Ammonia conditioning is employed here on one unit, but there is interest in liquid cohesivity additives as a safer alternative.

  2. The Efficiency Improvement by Combining HHO Gas, Coal and Oil in Boiler for Electricity Generation

    Directory of Open Access Journals (Sweden)

    Chia-Nan Wang

    2017-02-01

    Full Text Available Electricity is an essential energy that can benefit our daily lives. There are many sources available for electricity generation, such as coal, natural gas and nuclear. Among these sources, coal has been widely used in thermal power plants that account for about 41% of the worldwide electricity supply. However, these thermal power plants are also found to be a big pollution source to our environment. There is a need to explore alternative electricity sources and improve the efficiency of electricity generation. This research focuses on improving the efficiency of electricity generation through the use of hydrogen and oxygen mixture (HHO gas. In this research, experiments have been conducted to investigate the combined effects of HHO gas with other fuels, including coal and oil. The results show that the combinations of HHO with coal and oil can improve the efficiency of electricity generation while reducing the pollution to our environment.

  3. Analysis of Flue Gas Desulfurization (FGD) Processes for Potential Use on Army Coal-Fired Boilers

    Science.gov (United States)

    1980-09-01

    Rubber Co. FMC ( Soda Ash Plant ) General Motors General Motors General Motors General Motors General Motors Georgia-Pacific Paper Co. Great...use of alkali, especially caustic (NaOH), also requires increased concern with safety procedures for operating personnel. Limestone flue gas...proven technology was available at the time for SOx removal from stack gas at coal burning heating plants . This meant that coal burning units either

  4. Reconstruction design of medium pressure boiler fueling the blast furnace gas instead of coal powder%中压煤粉炉改燃高炉煤气改造设计

    Institute of Scientific and Technical Information of China (English)

    李涛

    2012-01-01

    为了节能和环保,钢铁企业自备电厂实施锅炉改造,将燃煤锅炉改燃高炉煤气.减少了高炉煤气放散,取得了锅炉效率高达88%的效果.%In order to energy conservation and environmental protection, steel - owned enterprises in the implementation of boiler plant have changed coal - fired boiler into a blast furnace gas - fired boiler. The blast furnace gas radiation was reduced, and the boiler efficiency was as high as 88%.

  5. FEASIBILITY ANALYSIS FOR INSTALLING A CIRCULATING FLUIDIZED BED BOILER FOR COFIRING MULTIPLE BIOFUELS AND OTHER WASTES WITH COAL AT PENN STATE UNIVERSITY

    Energy Technology Data Exchange (ETDEWEB)

    Bruce G. Miller; Sharon Falcone Miller; Robert Cooper; Douglas Donovan; John Gaudlip; Matthew Lapinsky; William Serencsits; Neil Raskin; Tom Steitz

    2002-10-14

    The Pennsylvania State University, under contract to the U.S. Department of Energy, National Energy Technology Laboratory is performing a feasibility analysis on installing a state-of-the-art circulating fluidized bed boiler and ceramic filter emission control device at Penn State's University Park campus for cofiring multiple biofuels and other wastes with coal, and developing a test program to evaluate cofiring multiple biofuels and coal-based feedstocks. The objective of the project is being accomplished using a team that includes personnel from Penn State's Energy Institute, Office of Physical Plant, and College of Agricultural Sciences; Foster Wheeler Energy Services, Inc.; Parsons Energy and Chemicals Group, Inc.; and Cofiring Alternatives. During this reporting period, the final technical design and cost estimate were submitted to Penn State by Foster Wheeler. In addition, Penn State initiated the internal site selection process to finalize the site for the boiler plant.

  6. 500 MW demonstration of advanced wall-fired combustion techniques for the reduction of nitrogen oxide emissions from coal-fired boilers

    Energy Technology Data Exchange (ETDEWEB)

    Sorge, J.N.; Larrimore, C.L.; Slatsky, M.D.; Menzies, W.R.; Smouse, S.M.; Stallings, J.W.

    1997-12-31

    This paper discusses the technical progress of a US Department of Energy Innovative Clean Coal Technology project demonstrating advanced wall-fired combustion techniques for the reduction of nitrogen oxide (NOx) emissions from coal-fired boilers. The primary objectives of the demonstration is to determine the long-term NOx reduction performance of advanced overfire air (AOFA), low NOx burners (LNB), and advanced digital control optimization methodologies applied in a stepwise fashion to a 500 MW boiler. The focus of this paper is to report (1) on the installation of three on-line carbon-in-ash monitors and (2) the design and results to date from the advanced digital control/optimization phase of the project.

  7. Engineering development of advanced coal-fired low-emission boiler systems. Technical progress report No. 15, April 15 1996--June 1996

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1996-08-19

    The Pittsburgh Energy Technology center of the US Department of Energy (DOE) has contracted with Combustion Engineering; Inc. (ABB CE) to perform work on the {open_quotes}Engineering Development of Advanced Coal-Fired Low-Emission Boiler Systems{close_quote} Project and has authorized ABB CE to complete Phase I on a cost-reimbursable basis and Phases II and III on a cost-share basis.

  8. FEASIBILITY ANALYSIS FOR INSTALLING A CIRCULATING FLUIDIZED BED BOILER FOR COFIRING MULTIPLE BIOFUELS AND OTHER WASTES WITH COAL AT PENN STATE UNIVERSITY

    Energy Technology Data Exchange (ETDEWEB)

    Bruce G. Miller; Sharon Falcone Miller; Robert Cooper; Douglas Donovan; John Gaudlip; Matthew Lapinsky; William Serencsits; Neil Raskin; Dale Lamke

    2001-10-12

    The Pennsylvania State University, under contract to the U.S. Department of Energy (DOE), National Energy Technology Laboratory (NETL) is performing a feasibility analysis on installing a state-of-the-art circulating fluidized bed (CFB) boiler and ceramic filter emission control device at Penn State's University Park campus for cofiring multiple biofuels and other wastes with coal, and developing a test program to evaluate cofiring multiple biofuels and coal-based feedstocks. Penn State currently operates an aging stoker-fired steam plant at its University Park campus and has spent considerable resources over the last ten to fifteen years investigating boiler replacements and performing life extension studies. This effort, in combination with a variety of agricultural and other wastes generated at the agricultural-based university and the surrounding rural community, has led Penn State to assemble a team of fluidized bed and cofiring experts to assess the feasibility of installing a CFB boiler for cofiring biomass and other wastes along with coal-based fuels.

  9. FEASIBILITY ANALYSIS FOR INSTALLING A CIRCULATING FLUIDIZED BED BOILER FOR COFIRING MULTIPLE BIOFUELS AND OTHER WASTES WITH COAL AT PENN STATE UNIVERSITY

    Energy Technology Data Exchange (ETDEWEB)

    Bruce G. Miller; Sharon Falcone Miller; Robert Cooper; Douglas Donovan; John Gaudlip; Matthew Lapinsky; William Serencsits; Neil Raskin; Tom Steitz

    2002-07-12

    The Pennsylvania State University, under contract to the U.S. Department of Energy (DOE), National Energy Technology Laboratory (NETL) is performing a feasibility analysis on installing a state-of-the-art circulating fluidized bed (CFB) boiler and ceramic filter emission control device at Penn State's University Park campus for cofiring multiple biofuels and other wastes with coal, and developing a test program to evaluate cofiring multiple biofuels and coal-based feedstocks. Penn State currently operates an aging stoker-fired steam plant at its University Park campus and has spent considerable resources over the last ten to fifteen years investigating boiler replacements and performing life extension studies. This effort, in combination with a variety of agricultural and other wastes generated at the agricultural-based university and the surrounding rural community, has led Penn State to assemble a team of fluidized bed and cofiring experts to assess the feasibility of installing a CFB boiler for cofiring biomass and other wastes along with coal-based fuels. The objective of the project is being accomplished using a team that includes personnel from Penn State's Energy Institute, Office of Physical Plant, and College of Agricultural Sciences; Foster Wheeler Energy Services, Inc.; Parsons Energy and Chemicals Group, Inc.; and Cofiring Alternatives.

  10. FEASIBILITY ANALYSIS FOR INSTALLING A CIRCULATING FLUIDIZED BED BOILER FOR COFIRING MULTIPLE BIOFUELS AND OTHER WASTES WITH COAL AT PENN STATE UNIVERSITY

    Energy Technology Data Exchange (ETDEWEB)

    Bruce G. Miller; Sharon Falcone Miller; Robert Cooper; Douglas Donovan; John Gaudlip; Matthew Lapinsky; William Serencsits; Neil Raskin; Dale Lamke; Joseph J. Battista

    2001-03-31

    The Pennsylvania State University, under contract to the U.S. Department of Energy (DOE), National Energy Technology Laboratory (NETL) is performing a feasibility analysis on installing a state-of-the-art circulating fluidized bed (CFB) boiler and ceramic filter emission control device at Penn State's University Park campus for cofiring multiple biofuels and other wastes with coal, and developing a test program to evaluate cofiring multiple biofuels and coal-based feedstocks. Penn State currently operates an aging stoker-fired steam plant at its University Park campus and has spent considerable resources over the last ten to fifteen years investigating boiler replacements and performing life extension studies. This effort, in combination with a variety of agricultural and other wastes generated at the agricultural-based university and the surrounding rural community, has led Penn State to assemble a team of fluidized bed and cofiring experts to assess the feasibility of installing a CFB boiler for cofiring biomass and other wastes along with coal-based fuels. The objective of the project is being accomplished using a team that includes personnel from Penn State's Energy Institute and the Office of Physical Plant, Foster Wheeler Energy Services, Inc., and Cofiring Alternatives.

  11. Pulverized Coal Fired Burner Using Coflow Jets with Velocity Difference in Revolving Kiln of Cement%回转水泥窑同向速差射流煤粉燃烧器

    Institute of Scientific and Technical Information of China (English)

    张拥军

    2000-01-01

    利用多股气体同向流动,人为控制气流的喷射速度,造成一定的速度差,借助射流的强烈的引射作用,使高温烟气回流至一次风、粉混合气流中,使一次风、粉提前加热、着火,从而强化了煤粉的燃烧,并保证了所需火焰的形状,解决了在回转水泥窑中大比例掺烧无烟煤的技术难题。%Using velocity difference among the multiple coflow jets and the strong entraiment effect of high speed jets,the high temperature flue will be recirculated to the exit of pulverized coal stream and mixed with the steam.The coal will be heated and ignited in advance,and thus the coal combustion will be intensified. Meanwhile the flame configuration can be ensured by using the present burner.Therefore the combustion of large amounts of anthrecite added to the bituminous coal is solved.

  12. 燃煤锅炉改造为燃气锅炉技术经济分析%Technical and Economic Analysis of Transforming Coal-Fired Boiler to Gas-Fired Boiler

    Institute of Scientific and Technical Information of China (English)

    万捷文

    2014-01-01

    To solve the contradiction of energy supply/demand and environmental pollution, the technology of transforming coal-fired boiler to gas-fired boiler has been discussed recently, and demonstrated by the technical and economic analysis combining with the engineering case. It points out that by choosing the alternative reasonably, the gas-fired Boiler is the main method of transforming coal-fired boiler, and it can meet the profits, environmental protection policy and energy policy as well.%伴随能源供需和环境污染的矛盾日益突出,在用燃煤锅炉进行天然气替代改造问题,引起管理部门和专家学者的关注,并进行了有益的研究。通过对燃煤锅炉的燃气替代中不同方案的技术经济分析,并结合工程实践,论证了燃煤锅炉天然气替代的经济性和可行性。结论表明,通过合理选择替代方案和工程实施,天然气锅炉能符合企业经济利益和社会环保政策、能源政策的发展趋势,是目前锅炉建设及改造的主要方向。

  13. 燃煤电站锅炉碳化硅质卫燃带表面结渣行为%Slagging Behavior on Surface of Carborundum-based Refractory Liner in a Coal-fired Boiler

    Institute of Scientific and Technical Information of China (English)

    何金桥; 鄢晓忠; 陈冬林

    2011-01-01

    采用扫描电镜、能谱分析仪和X射线衍射等方法对燃煤电站锅炉SiC质卫燃带上结渣的渣样进行了测试,并就渣样的形貌、结晶物相转化特性及其渣样成分分布进行了分析研究.结果表明:煤颗粒的不充分燃烧造成碱性金属阳离子向SiC耐火板侧发生扩散,但难以穿过耐火板表层的SiO2保护膜,从而与SiC质卫燃带通过机械结合的方式相互黏结在一起;方晶石和鳞石英易与耐火板发生熔融冶金结合,形成较强的黏结作用,但是耐火板处熔融的片状鳞石英和方晶石含量较少,因此渣、板之间总体的黏结作用较弱.%In order to study the coal ash slagging behavior on surface of carborundum-based refractory liner in a coal-fired boiler, slag samples taking from the liner were investigated by Scanning Electron Microscopy (SEM), Energy Dispersive Spectrometer (EDS) and X-ray diffraction(XRD), during which the specific morphology, phase transformation and component distribution were analyzed. Results show that the in- complete combustion of pulverized coal makes alkaline metal ion diffuse to the refractory liner, which then sticks on the liner mechanically, because it is hard to permeate through the SiO2 protective film covering the liner. Metallurgical bonding lies between the cristobalite/tridymite and the liner, and the bonding be- tween plate-like tridymite and the liner is very strong. Since the content of plate-like tridymite in the slag is very little, so the comprehesive bonding force is relatively weak between the slag and the liner.

  14. Estimation of capability of changing the boilers TP-14A at Kumertau Termal Power Station to burning B3 grade coal from Verkhne-Sokursky deposit

    Science.gov (United States)

    Supranov, V. M.; Shtegman, A. V.; Fomenko, E. A.

    2016-04-01

    Currently, TP-14A boilers should be changed into burning off-design fuel: grade B3 coal of Verkhne-Sokursky deposit. Its share (by heat) in the fuel balance should be not less than 80%. A test burning of Verkhne-Sokursky coal was carried out, which showed that, in its present form, the boilers and dust-systems are not suitable to operate with this fuel, because their characteristics significantly differs from the project one. It is impossible to maintain the overheating temperature at the required level during operation on only coal; it is difficult to maintain the temperature behind the mills at the level of 200°C. The joint burning the coal with natural gas allows to solve these problems at operation of one or two mills. However, substantial fuel underburning, essential thermal maldistributions on the steam flows, and emissions of NO x above permissible values is observed. Based on the results of test burning and joint calculations of furnace, boiler, and dust-systems, ways to solve these problems were developed. For modeling the furnace process, the Fluent and Sigma Flame software were used. Adapted mathematical models of the boiler and dust-preparing systems were created using the Boiler Designer and Stoker software. It is necessary to reconstruct the boiler plants, which can perform in two stages. In the first stage, the existing burners are replaced by the burners with turning nozzles and two-stage burning is arranged, and the inertial separators and recirculation of the drying agent are installed on the mills. In the second stage, the change to concentric burning is carried out, the heating surface of radiation part of the steam superheater increases, and the preset included hammer part is installed at the mill. It is shown that a positive effect should be obtained already after the first stage of reconstruction. The second stage of reconstruction will require additional expenses, but its implementation will allow to a greater extent to eliminate the

  15. Innovative Clean Coal Technology (ICCT): Demonstration of Selective Catalytic Reduction (SCR) technology for the control of nitrogen oxide (NO{sub x}) emissions from high-sulfur coal-fired boilers. Third quarterly technical progress report 1992

    Energy Technology Data Exchange (ETDEWEB)

    1992-11-01

    The objective of this project is to demonstrate and evaluate commercially available Selective Catalytic Reduction (SCR) catalysts from US, Japanese and European catalyst suppliers on a high-sulfur US coal-fired boiler. SCR is a post-combustion nitrogen oxide (NO{sub x}) control technology that involves injecting ammonia into the flue gas generated from coal combustion in an electric utility boiler. The flue gas containing ammonia is then passed through a reactor that contains a specialized catalyst. In the presence of the catalyst, the ammonia reacts with NO{sub x} to convert it to nitrogen and water vapor. Although SCR is widely practiced in Japan and Europe on gas-, oil-, and low-sulfur, coal-fired boilers, there are several technical uncertainties associated with applying SCR to US coals. These uncertainties include: (1) potential catalyst deactivation due to poisoning by trace metal species present in US coals that are not present in other fuels. (2) performance of the technology and effects on the balance-of-plant equipment in the presence of high amounts of SO{sub 2} and SO{sub 3} and (3) performance of a wide variety of SCR catalyst compositions, geometries and methods of manufacture under typical high-sulfur coal-fired utility operating conditions. These uncertainties will be explored by constructing a series of small- scale SCR reactors and simultaneously exposing different SCR catalysts to flue gas derived from the combustion of high-sulfur US coal. The demonstration will be performed at Gulf Power Company`s Plant Crist Unit No. 5 (75 MW capacity) near Pensacola, Florida.

  16. Innovative Clean Coal Technology (ICCT): Demonstration of selective catalytic reduction (SCR) technology for the control of nitrogen oxide (NO{sub x}) emissions from high-sulfur coal-fired boilers. Technical progress report, third and fourth quarters 1994

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1995-11-01

    The objective of this project is to demonstrate and evaluate commercially available selective catalytic reduction (SCR) catalysts from U.S., Japanese, and European catalyst suppliers on a high-sulfur U.S. Coal-fired boiler. SCR is a post-combustion nitrogen oxide (NO{sub x}) control technology that involves injecting ammonia into the flue gas generated from coal combustion in an electric utility boiler. The flue gas containing ammonia is then passed through a reactor that contains a specialized catalyst. In the presence of the catalyst, the ammonia reacts with NO{sub x} to form nitrogen and water vapor. Although SCR is widely practiced in Japan and European gas-, oil-, and low-sulfur coal-fired boilers, there are several technical uncertainties associated with applying SCR to U.S. coals. These uncertainties include: (1) potential catalyst deactivation due to poisoning by trace metal species present in U.S. coals that are not present in other fuels; (2) performance of the technology and effects on the balance-of-plant equipment in the presence of high amounts of SO{sub 2} and SO{sub 3}; performance of a wide variety of SCR catalyst compositions, geometries, and methods of manufacture under typical high-sulfur coal-fired utility operating conditions. These uncertainties are being explored by operating a series of small- scale SCR reactors and simultaneously exposing different SCR catalysts to flue gas derived from the combustion of high sulfur U.S. coal. The demonstration is being performed at Gulf Power Company`s Plant Crist Unit No. 5 (75 MW capacity) near Pensacola, Florida. The project is funded by the U.S. Department of Energy (DOE), Southern Company Services, Inc. (SCS on behalf of the entire Southern electric system), the Electric Power Research Institute (EPRI), and Ontario Hydro. SCS is the participant responsible for managing al aspects of this project. 1 ref., 69 figs., 45 tabs.

  17. Innovative Clean Coal Technology (ICCT): Demonstration of selective catalytic reduction (SCR) technology for the control of nitrogen oxide (NO{sub x}) emissions from high-sulfur coal-fired boilers. Technical progress report, October 1993--December 1993

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1995-06-01

    The objective of this project is to demonstrate and evaluate commercially available Selective Catalytic Reduction (SCR) catalysts from U.S., Japanese and European catalyst suppliers on a high-sulfur U.S. coal-fired boiler. SCR is a post-combustion nitrogen oxide (NO{sub x}) control technology that involves injecting ammonia into the flue gas generated from coal combustion in an electric utility boiler. The flue gas containing ammonia is then passed through a reactor that contains a specialized catalyst. In the presence of the catalyst, the ammonia reacts with NO{sub x} to convert it to nitrogen and water vapor. Although SCR is widely practiced in Japan and Europe on gas-, oil-, and low-sulfur coal-fired boilers, there are several technical uncertainties associated with applying SCR to U.S. coals. These uncertainties include: (1) potential catalyst deactivation due to poisoning by trace metal species present in U.S. coals that are not present in other fuels; (2) performance of the technology and effects on the balance-of-plant equipment in the presence of high amounts of SO{sub 2} and SO{sub 3}; and (3) performance of a wide variety of SCR catalyst compositions, geometries and methods of manufacture under typical high-sulfur coal-fired utility operating conditions. These uncertainties are being explored by operating a series of small-scale SCR reactors and simultaneously exposing different SCR catalysts to flue gas derived from the combustion of high sulfur U.S. coal.

  18. Innovative Clean Coal Technology (ICCT): Demonstration of Selective Catalytic Reduction (SCR) technology for the control of nitrogen oxide (NO[sub x]) emissions from high-sulfur coal-fired boilers

    Energy Technology Data Exchange (ETDEWEB)

    1992-11-01

    The objective of this project is to demonstrate and evaluate commercially available Selective Catalytic Reduction (SCR) catalysts from US, Japanese and European catalyst suppliers on a high-sulfur US coal-fired boiler. SCR is a post-combustion nitrogen oxide (NO[sub x]) control technology that involves injecting ammonia into the flue gas generated from coal combustion in an electric utility boiler. The flue gas containing ammonia is then passed through a reactor that contains a specialized catalyst. In the presence of the catalyst, the ammonia reacts with NO[sub x] to convert it to nitrogen and water vapor. Although SCR is widely practiced in Japan and Europe on gas-, oil-, and low-sulfur, coal-fired boilers, there are several technical uncertainties associated with applying SCR to US coals. These uncertainties include: (1) potential catalyst deactivation due to poisoning by trace metal species present in US coals that are not present in other fuels. (2) performance of the technology and effects on the balance-of-plant equipment in the presence of high amounts of SO[sub 2] and SO[sub 3] and (3) performance of a wide variety of SCR catalyst compositions, geometries and methods of manufacture under typical high-sulfur coal-fired utility operating conditions. These uncertainties will be explored by constructing a series of small- scale SCR reactors and simultaneously exposing different SCR catalysts to flue gas derived from the combustion of high-sulfur US coal. The demonstration will be performed at Gulf Power Company's Plant Crist Unit No. 5 (75 MW capacity) near Pensacola, Florida.

  19. Innovative Clean Coal Technology (ICCT). Demonstration of Selective Catalytic Reduction (SCR) technology for the control of nitrogen oxide (NO{sub x}) emissions from high-sulfur coal-fired boilers: Volume 1. Final report

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1996-10-01

    The objective of this project is to demonstrate and evaluate commercially available Selective Catalytic Reduction (SCR) catalysts from U.S., Japanese and European catalyst suppliers on a high-sulfur U.S. coal-fired boiler. SCR is a post-combustion nitrogen oxide (NO.) control technology that involves injecting ammonia into the flue gas generated from coal combustion in an electric utility boiler. The flue gas containing ammonia is then passed through a reactor that contains a specialized catalyst. In the presence of the catalyst, the ammonia reacts with NO. to convert it to nitrogen and water vapor. Although SCR is widely practiced in Japan and Europe on gas-, oil-, and low-sulfur coal- fired boilers, there are several technical uncertainties associated with applying SCR to U.S. coals. These uncertainties include: 1) potential catalyst deactivation due to poisoning by trace metal species present in U.S. coals that are not present in other fuels. 2) performance of the technology and effects on the balance-of- plant equipment in the presence of high amounts of SO{sub 2} and SO{sub 3}. 3) performance of a wide variety of SCR catalyst compositions, geometries and methods of manufacturer under typical high-sulfur coal-fired utility operating conditions. These uncertainties were explored by operating nine small-scale SCR reactors and simultaneously exposing different SCR catalysts to flue gas derived from the combustion of high sulfur U.S. coal. In addition, the test facility operating experience provided a basis for an economic study investigating the implementation of SCR technology.

  20. Innovative Clean Coal Technology (ICCT): Demonstration of selective catalytic reduction technology for the control of nitrogen oxide emissions from high-sulfur coal-fired boilers. First and second quarterly technical progress reports, [January--June 1995]. Final report

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1995-12-31

    The objective of this project is to demonstrate and evaluate commercially available Selective Catalytic Reduction (SCR) catalysts from US, Japanese and European catalyst suppliers on a high-sulfur US coal-fired boiler. SCR is a post-combustion nitrogen oxide (NO{sub x}) control technology that involves injecting ammonia (NH{sub 3}) into the flue gas generated from coal combustion in an electric utility boiler. The flue gas containing ammonia is then passed through a reactor containing a specialized catalyst. In the presence of the catalyst, the ammonia reacts with NO{sub x} to convert it to nitrogen and water vapor. Although SCR is widely practiced in Japan and Europe on gas-, oil-, and low-sulfur coal-fired boilers, there are several technical uncertainties associated with applying SCR to US coals. These uncertainties include: (1) potential catalyst deactivation due to poisoning by trace metal species present in US coals that are not present in other fuels. (2) performance of the technology and effects on the balance-of-plant equipment in the presence of high amounts of SO{sub 2} and SO{sub 3}. (3) performance of a wide variety of SCR catalyst compositions, geometries, and methods of manufacture under typical high-sulfur coal-fired utility operating conditions. These uncertainties are being explored by operating a series of small-scale SCR reactors and simultaneously exposing different SCR catalysts to flue gas derived from the combustion of high sulfur US coal. The demonstration is being performed at Gulf Power Company`s Plant Crist Unit No. 5 (75 MW nameplate capacity) near Pensacola, Florida. The project is funded by the US Department of Energy (DOE), Southern Company Services, Inc. (SCS on behalf of the entire Southern electric system), the Electric Power Research Institute (EPRI), and Ontario Hydro. SCS is the participant responsible for managing all aspects of this project.

  1. Numerical investigation on the flow, combustion, and NOX emission characteristics in a 660 MWe tangential firing ultra-supercritical boiler

    Directory of Open Access Journals (Sweden)

    Wenjing Sun

    2016-02-01

    Full Text Available A three-dimensional numerical simulation was carried out to study the pulverized-coal combustion process in a tangentially fired ultra-supercritical boiler. The realizable k-ε model for gas coupled with discrete phase model for coal particles, P-1 radiation model for radiation, two-competing-rates model for devolatilization, and kinetics/diffusion-limited model for combustion process are considered. The characteristics of the flow field, particle motion, temperature distribution, species components, and NOx emissions were numerically investigated. The good agreement of the measurements and predictions implies that the applied simulation models are appropriate for modeling commercial-scale coal boilers. It is found that an ideal turbulent flow and particle trajectory can be observed in this unconventional pulverized-coal furnace. With the application of over-fire air and additional air, lean-oxygen combustion takes place near the burner sets region and higher temperature at furnace exit is acquired for better heat transfer. Within the limits of secondary air, more steady combustion process is achieved as well as the reduction of NOx. Furthermore, the influences of the secondary air, over-fire air, and additional air on the NOx emissions are obtained. The numerical results reveal that NOx formation attenuates with the decrease in the secondary air ratio (γ2nd and the ratio of the additional air to the over-fire air (γAA/γOFA was within the limits.

  2. Ash transformation in suspension fired boilers co-firing coal and straw

    DEFF Research Database (Denmark)

    Zheng, Yuanjing; Jensen, Peter Arendt; Jensen, Anker Degn

    reactor experiments with co-firing of coal and straw, making mineral and alkali vapor laboratory reactor experiments and by developing a model of KCl reaction with kaolin. The results include correlations that can be used to estimate the speciation of potassium in the fly ash when co-firing straw...

  3. TENORM: Coal Combustion Residuals

    Science.gov (United States)

    Burning coal in boilers to create steam for power generation and industrial applications produces a number of combustion residuals. Naturally radioactive materials that were in the coal mostly end up in fly ash, bottom ash and boiler slag.

  4. Mechanical Properties of High Strength Concrete Containing Coal Bottom Ash and Oil-Palm Boiler Clinker as Fine Aggregates

    Directory of Open Access Journals (Sweden)

    Soofinajafi Mahmood

    2016-01-01

    Full Text Available This research aims to utilize Coal Furnace Bottom ash (CBA and Oil-Palm Boiler Clinker (OPBC as fine aggregate in concrete mix proportions. They are solid wastes from power plant and Oil Palm industry, respectively. Since these by-products do not have any primary use and are pure waste, an opportunity to use them as aggregate in concrete industry not only is economical but also will be an environmental friendly opportunity leading towards a more sustainable production chain. CBA and OPBC sands had similar grading to normal sand but have lower density and higher water absorption. In a high strength concrete, normal sand was replaced up to 25% with either CBA or OPBC. Test results showed that although water absorption of these wastes was more than normal sand but the slump value of concrete containing each of these wastes showed that these concretes had good workability. All mixes containing these wastes had slightly lower compressive strength at early ages and equivalent or higher compressive strength at later ages compared to control mix. The 28-day compressive strength of these concretes was in the range of 69–76 MPa which can be categorized as high strength concrete. In general, the performance of OPBC was better than CBA at 25% replacement level. However, it is recommended that at least 12.5% of total volume of fine aggregate in a high strength concrete is used of CBA or OPBC.

  5. ADVANCED FLUE GAS CONDITIONING AS A RETROFIT UPGRADE TO ENHANCE PM COLLECTION FROM COAL-FIRED ELECTRIC UTILITY BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    Kenneth E. Baldrey

    2001-09-01

    The U.S. Department of Energy and ADA Environmental Solutions are engaged in a project to develop commercial flue gas conditioning additives. The objective is to develop conditioning agents that can help improve particulate control performance of smaller or under-sized electrostatic precipitators on utility coal-fired boilers. The new chemicals will be used to control both the electrical resistivity and the adhesion or cohesivity of the fly ash. There is a need to provide cost-effective and safer alternatives to traditional flue gas conditioning with SO{sub 3} and ammonia. During this reporting quarter, further laboratory-screening tests of additive formulations were completed. For these tests, the electrostatic tensiometer method was used for determination of fly ash cohesivity. Resistivity was measured for each screening test with a multi-cell laboratory fly ash resistivity furnace constructed for this project. Also during this quarter chemical formulation testing was undertaken to identify stable and compatible resistivity/cohesivity liquid products.

  6. ADVANCED FLUE GAS CONDITIONING AS A RETROFIT UPGRADE TO ENHANCE PM COLLECTION FROM COAL-FIRED ELECTRIC UTILITY BOILERS

    Energy Technology Data Exchange (ETDEWEB)

    Kenneth E. Baldrey

    2001-05-01

    The U.S. Department of Energy and ADA Environmental Solutions has begun a project to develop commercial flue gas conditioning additives. The objective is to develop conditioning agents that can help improve particulate control performance of smaller or under-sized electrostatic precipitators on utility coal-fired boilers. The new chemicals will be used to control both the electrical resistivity and the adhesion or cohesivity of the flyash. There is a need to provide cost-effective and safer alternatives to traditional flue gas conditioning with SO{sub 3} and ammonia. During the fourth reporting quarter, laboratory-screening tests of more than 20 potential additive formulations were completed. For these tests, the electrostatic tensiometer method was used for determination of flyash cohesivity. Resistivity was measured for each screening test with a new multi-cell laboratory flyash resistivity furnace constructed for this project. An initial field trial of three additive formulations was also conducted at the City of Ames, Iowa Municipal Power Plant.

  7. PIV measurements of the turbulence integral length scale on cold combustion flow field of tangential firing boiler

    Energy Technology Data Exchange (ETDEWEB)

    Wu, Wen-fei; Xie, Jing-xing; Gong, Zhi-jun; Li, Bao-wei [Inner Mongolia Univ. of Science and Technology, Baotou (China). Inner Mongolia Key Lab. for Utilization of Bayan Obo Multi-Metallic Resources: Elected State Key Lab.

    2013-07-01

    The process of the pulverized coal combustion in tangential firing boiler has prominent significance on improving boiler operation efficiency and reducing NO{sub X} emission. This paper aims at researching complex turbulent vortex coherent structure formed by the four corners jets in the burner zone, a cold experimental model of tangential firing boiler has been built. And by employing spatial correlation analysis method and PIV (Particle Image Velocimetry) technique, the law of Vortex scale distribution on the three typical horizontal layers of the model based on the turbulent Integral Length Scale (ILS) has been researched. According to the correlation analysis of ILS and the temporal average velocity, it can be seen that the turbulent vortex scale distribution in the burner zone of the model is affected by both jet velocity and the position of wind layers, and is not linear with the variation of jet velocity. The vortex scale distribution of the upper primary air is significantly different from the others. Therefore, studying the ILS of turbulent vortex integral scale is instructive to high efficiency cleaning combustion of pulverized coal in theory.

  8. 恩德粉煤气化装置空喷塔改造工艺计算%Process Calculation of Reformation for Empty Spray Tower in Ende Pulverized Coal Gasification Plant

    Institute of Scientific and Technical Information of China (English)

    姜天夫

    2012-01-01

    Author has introduced the technical reformation scheme for the empty scrubber in Ende pulverized coal gasification plant and its process de- sign calculation principle ; the running effect indicates after reformation that the outlet temperature of water can be reduced from 60℃to 48℃, the con- tinuously running time of the empty scrubber is increased from less than 60 days to 100 days.%介绍了恩德粉煤气化装置空心洗涤塔的技术改造方案及其工艺设计计算过程;改造后的运行效果表明,出水温度由60℃降低到48℃,空心洗涤塔连续运行时间由不到60天增加到100天。

  9. Technical and Economic Aspects of Biomass Co-Firing in Coal-Fired Boilers

    Directory of Open Access Journals (Sweden)

    Dzikuć M.

    2014-11-01

    Full Text Available The article presents the analysis of the potential of using biomass and coal co-firing in the Polish electro energetic system and shows the benefits resulting from an increase of biomass amount in electricity production in one of the largest Polish power stations. The paper discusses the most often used technologies for biomass co-firing and the potential of using biomass in electricity production in Poland. It also emphasises the fact that biomass co-firing allows a reduction of greenhouse gases emissions to the atmosphere and helps decrease consumption of energy resources. The article also emphasises the economic meaning of increasing the share of renewable energy resources in energy balance, including biomass, due to costs related to greenhouse gases emissions charges. Finally, conclusions from using biomass and coal co-firing in electricity production are presented

  10. Effect of tertiary air speed on combustion efficiency of pulverized coal burners%三次风速对煤粉燃烧器燃烧效率的影响

    Institute of Scientific and Technical Information of China (English)

    张文学; 郭彩; 武建新

    2015-01-01

    In order to study the influence of tertiary alr speed on burning efficiency of LB2000 type asphalt mixing station pulverized coal burners,a mathematical model was established.By using the Fluent software and the standard k-εmodel,numerical simulation on pulverized coal combustion in the burner was carried out.With different tertiary alr speeds,the temperature field,component concentration field,burning rate distribution field and particle traj ectory in the buerner were studied.According to the evaluation standard of combustion efficiency,the optimal tertiary alr speed should be from 40 m/s to 50 m/s.%为了研究三次风速对LB2000型沥青搅拌站煤粉燃烧器燃烧效率的影响,建立煤粉燃烧器数学模型,应用Fluent软件,采用标准k-ε模型对煤粉燃烧器中的煤粉燃烧进行模拟.在不同三次风风速下,对沥青搅拌站煤粉燃烧器的温度场、组分浓度场、燃尽率分布场和颗粒轨迹进行了分析.根据燃烧效率评价标准,得出了最佳三次风风速为40~50 m/s.

  11. Achievement report for fiscal 1999 on project for supporting the formation of energy/environmental technology verification project. International joint verification research project (Verification project relative to ignition and NOx reduction using plasma sub-burner in pulverized coal-fired furnace); 1999 nendo plasma sabubana ni yoru bifuntan nenshoro ni okeru chakka oyobi NO{sub x} teigen gijutsu ni kansuru jissho project seika hokokusho

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    2000-03-01

    This project is executed through the cooperation of a Russian research institute, Akita Prefectural University, and the Ishikawajima-Harima Heavy Industries Co., Ltd. In the development of a plasma sub-burner and the basic research for its verification, a pulverized coal burning plasma sub-burner is designed and fabricated, a basic burning experiment is conducted for the plasma sub-burner, and plasma stabilization in a pulverized coal flow is simulated. In the verification study of the ignition by the plasma sub-burner in a pulverized coal-fired furnace, it is found that the newly-developed plasma sub-burner satisfies the prescribed operating conditions in the system and that the ignition of pulverized coal takes place across the air ratio range of 0.5-1.5 when pulverized coal is fed to the sub-burner. It is also found that NOx is reduced a great deal when a plasma operating on an orifice gas of air or nitrogen is generated in a gas which contains NOx. (NEDO)

  12. Optimization of the process of plasma ignition of coal

    Energy Technology Data Exchange (ETDEWEB)

    Peregudov, V.S. [Russian Academy of Sciences, Novosibirsk (Russian Federation)

    2009-04-15

    Results are given of experimental and theoretical investigations of plasma ignition of coal as a result of its thermochemical preparation in application to the processes of firing up a boiler and stabilizing the flame combustion. The experimental test bed with a commercial-scale burner is used for determining the conditions of plasma ignition of low-reactivity high-ash anthracite depending on the concentration of coal in the air mixture and velocity of the latter. The calculations produce an equation (important from the standpoint of practical applications) for determining the energy expenditure for plasma ignition of coal depending on the basic process parameters. The tests reveal the difficulties arising in firing up a boiler with direct delivery of pulverized coal from the mill to furnace. A scheme is suggested, which enables one to reduce the energy expenditure for ignition of coal and improve the reliability of the process of firing up such a boiler. Results are given of calculation of plasma thermochemical preparation of coal under conditions of lower concentration of oxygen in the air mixture.

  13. Innovative clean coal technology (ICCT): Demonstration of selective catalytic reduction (SCR) technology for the control of nitrogen oxide (NO{sub x}) emissions from high-sulfur coal-fired boilers. Fourth quarterly progress report

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1992-12-31

    The objective of this project is to demonstrate and evaluate commercially available Selective Catalytic Reduction (SCR) catalysts from US, Japanese and European catalyst suppliers on a high-sulfur US coal-fired boiler. SC