WorldWideScience

Sample records for clean coke process

  1. Principles of processes used for coal gas cleaning and recovery of chemical products of coking. Part II. [Poland

    Energy Technology Data Exchange (ETDEWEB)

    Ulatowski, R.

    1983-02-01

    This paper discusses removal of tars, ammonia, benzene and desulfurization of coal gas from black coal coking. About 30% of coal gas produced by coking plants in Poland is desulfurized. The average content of hydrogen sulfide in coal gas ranges from 6 to 8 g/m/sup 3/. After desulfurization hydrogen sulfur content does not exceed 0.2 g/m/sup 3/. Two processes are used in Poland for coal gas desulfurization: the vacuum carbonate process and the Thylox process. Chemical reactions during gas desulfurization with the two processes are discussed. Regeneration systems, productivity and efficiency of gas desulfurization using the two processes are compared. The following processes used in other countries are comparatively evaluated: the Fumaks-Rodax process in Japan, the Perox process, the Stretford process, the Sulfiban process in the USA and the Claus process.

  2. Brown coal coke in biological waste water cleaning

    International Nuclear Information System (INIS)

    Biological sewage plants working by the activated sludge process are often confronted by the following problems: the formation of expanded bubbles, lack of decomposition performance, unstable operation and insufficient excess sludge dewatering. In the former East Germany, there is also the problem of too little nitrificaion/denitrification, caused by obsolete plant. The use of brown coal coke guarantees efficient cleaning of waste water. (orig.)

  3. Experimental study on shrinkage characteristics of semi-coke/coke under gradient temperature during coking process

    Energy Technology Data Exchange (ETDEWEB)

    Fu, Z.; Guo, Z.; Wang, S. [Chinese Academy of Sciences, Beijing (China)

    2006-04-15

    A furnace equipped with a removable measuring scale in the side was applied to study on the shrinkage characteristics of semi-coke/coke under gradient temperature during coking process. 1500 g coking coal was used in the test. The effects of coking time, central temperature, heating-up rate and gradient temperature on lateral shrinkage were studied under different heating rate. The results show that the coal begins to shrink at a central temperature range of 280 to 360{sup o}C and ends at about 900{sup o}C. The lateral shrinkage is in a range of 5 mm to 8.5 mm and lateral shrinkage ratio is 7 to 12%. Generally, the gradient temperature increases and lateral shrinkage decreases with increasing heating-up rate and density. The central temperature of beginning shrinkage, the second shrinkage peak, gradient temperature of different locations and shrinkage coefficient of coal decreases with the increase of heating rate. The central temperature of beginning shrinkage and gradient temperature of different locations increase with increasing density. But the increase of density has no influence on shrinkage coefficient and shrinkage peak. In addition, the temperature rise rates at different locations are different during different coking stages. 9 refs., 9 figs., 1 tab.

  4. Nitrogen Chemistry and Coke Transformation of FCC Coked Catalyst during the Regeneration Process

    OpenAIRE

    Junjun Shi; Jianyu Guan; Dawei Guo; Jiushun Zhang; Liam John France; Lefu Wang; Xuehui Li

    2016-01-01

    Regeneration of the coked catalyst is an important process of fluid catalytic cracking (FCC) in petroleum refining, however, this process will emit environmentally harmful gases such as nitrogen and carbon oxides. Transformation of N and C containing compounds in industrial FCC coke under thermal decomposition was investigated via TPD and TPO to examine the evolved gaseous species and TGA, NMR and XPS to analyse the residual coke fraction. Two distinct regions of gas evolution are observed du...

  5. NUMERICAL SIMULATION FOR A PROCESS ANALYSIS OF A COKE OVEN

    Institute of Scientific and Technical Information of China (English)

    Zhancheng Guo; Huiqing Tang

    2005-01-01

    A computational fluid dynamic model is established for a coking process analysis of a coke oven using PHOENICS CFD package. The model simultaneously calculates the transient composition, temperatures of the gas and the solid phases, velocity of the gas phase and porosity and density of the semi-coke phase. Numerical simulation is illustrated in predicting the evolution of volatile gases, gas flow paths, profiles of density, porosity of the coke oven charge,profiles of temperatures of the coke oven gas and the semi-coke bed. On the basis of above modeling, the flow of coke oven gas (COG) blown from the bottom of the coke oven into the porous semi-coke bed is simulated to reveal whether or not and when the blown COG can uniformly flow through the porous semi-coke bed for the purpose of desulfurizing the semi-coke by recycling the COG. The simulation results show that the blown COG can uniformly flow through the semi-coke bed only after the temperature at the center of the semi-coke bed has risen to above 900 ℃.

  6. The Corex process - ironmaking without coke

    Energy Technology Data Exchange (ETDEWEB)

    Flickenschild, J.; Hauk, R. (Deutsche Voest-Alpine Industrieanlagenbau GmbH Duesseldorf (Germany, F.R.))

    1990-12-01

    The high cost of coke making and the environmental problems involved as well as the increasing price of natural gas for DRI production were the reasons for the development of the COREX process for the production of hot metal based on a wide range of ordinary steam coals. After the successful operation of a CORX pilot plant, the first commercial plant was built at Iscor in Pretoria, South Africa, and is now in full operation. 3 refs., 9 figs., 17 tabs.

  7. Fluid coking : a competitive option for heavy feed processing

    International Nuclear Information System (INIS)

    Fluid coking is a proven thermal conversion process for converting heavy hydrocarbon feeds to lighter products. Fluid coking was commercialized by Exxon over 40 years ago. A total of 13 units have been built with over 330 years of cumulative operating experience. Fluid coking can process many different feeds at once and is usually insensitive to feed contaminants such as sulfur, nitrogen and metals. New developments in coke utilization and flue gas desulfurization/departiculation have prompted new economic studies. Fluid coking is competitive and is the most attractive option compared to delayed coking, particularly for very heavy feed stocks such as deasphalter bottoms. Viewgraphs describe the fluid coking process, its advantages, utilization, and commercial viability. 7 tabs., 3 figs

  8. Closed-cycle process of coke-cooling water in delayed coking unit

    International Nuclear Information System (INIS)

    Synthesized processes are commonly used to treat coke-cooling wastewater. These include cold coke-cut water, diluting coke-cooling water, adding chemical deodorization into oily water, high-speed centrifugal separation, de-oiling and deodorization by coke adsorption, and open nature cooling. However, because of water and volatile evaporation loss, it is not suitable to process high-sulphur heavy oil using open treatments. This paper proposed a closed-cycling process in order to solve the wastewater treatment problem. The process is based on the characteristics of coke-cooling water, such as rapid parametric variation, oil-water-coke emulsification and steam-water mixing. The paper discussed the material characteristics and general idea of the study. The process of closed-cycle separation and utilization process of coke-cooling water was presented along with a process flow diagram. Several applications were presented, including a picture of hydrocyclones for pollution separation and a picture of equipments of pollution separation and components regeneration. The results showed good effect had been achieved since the coke-cooling water system was put into production in 2004. The recycling ratios for the components of the coke-cooling water were 100 per cent, and air quality in the operating area reached the requirements of the national operating site circumstance and the health standards. Calibration results of the demonstration unit were presented. It was concluded that since the devices went into operation, the function of production has been normal and stable. The operation was simple, flexible, adjustable and reliable, with significant economic efficiency and environmental benefits. 10 refs., 2 tabs., 3 figs

  9. Parameters and evaluation criteria for the coal coking process

    Energy Technology Data Exchange (ETDEWEB)

    Postrzednik, S.

    1988-09-01

    Analyzes effects of temperature distribution on black coal coking in a conventional coke oven. Two parameters are used for description of temperature distribution: a local (time-average) divergence function and an instant (volumetric) divergence function. Formulae for determining the two parameters are derived. Use of the mean values of the two functions as an evaluation criteria for assessment of the coking process is recommended. Practical use of the proposed criteria is discuussed. 8 refs.

  10. Process for the preparation of isotropic petroleum coke

    International Nuclear Information System (INIS)

    A description is given of a process for preparing isotropic coke from oil residue charge. It includes blowing air into the residue until it reaches a softening temperature of around 49 to 116 deg C, the deferred coking of the residue having undergone blowing at a temperature of around 247 to 640 deg C, at a pressure between around 1.38x105 and 1.72x106 Pa, and the recovery of isotropic coke with a thermal expansion coefficient ratio under 1.5 approximately. The isotropic coke is used for preparing hexagonal graphite bars for nuclear reactor moderators

  11. Nitrogen Chemistry and Coke Transformation of FCC Coked Catalyst during the Regeneration Process

    Science.gov (United States)

    Shi, Junjun; Guan, Jianyu; Guo, Dawei; Zhang, Jiushun; France, Liam John; Wang, Lefu; Li, Xuehui

    2016-06-01

    Regeneration of the coked catalyst is an important process of fluid catalytic cracking (FCC) in petroleum refining, however, this process will emit environmentally harmful gases such as nitrogen and carbon oxides. Transformation of N and C containing compounds in industrial FCC coke under thermal decomposition was investigated via TPD and TPO to examine the evolved gaseous species and TGA, NMR and XPS to analyse the residual coke fraction. Two distinct regions of gas evolution are observed during TPD for the first time, and they arise from decomposition of aliphatic carbons and aromatic carbons. Three types of N species, pyrrolic N, pyridinic N and quaternary N are identified in the FCC coke, the former one is unstable and tends to be decomposed into pyridinic and quaternary N. Mechanisms of NO, CO and CO2 evolution during TPD are proposed and lattice oxygen is suggested to be an important oxygen resource. Regeneration process indicates that coke-C tends to preferentially oxidise compared with coke-N. Hence, new technology for promoting nitrogen-containing compounds conversion will benefit the in-situ reduction of NO by CO during FCC regeneration.

  12. Nitrogen Chemistry and Coke Transformation of FCC Coked Catalyst during the Regeneration Process

    Science.gov (United States)

    Shi, Junjun; Guan, Jianyu; Guo, Dawei; Zhang, Jiushun; France, Liam John; Wang, Lefu; Li, Xuehui

    2016-01-01

    Regeneration of the coked catalyst is an important process of fluid catalytic cracking (FCC) in petroleum refining, however, this process will emit environmentally harmful gases such as nitrogen and carbon oxides. Transformation of N and C containing compounds in industrial FCC coke under thermal decomposition was investigated via TPD and TPO to examine the evolved gaseous species and TGA, NMR and XPS to analyse the residual coke fraction. Two distinct regions of gas evolution are observed during TPD for the first time, and they arise from decomposition of aliphatic carbons and aromatic carbons. Three types of N species, pyrrolic N, pyridinic N and quaternary N are identified in the FCC coke, the former one is unstable and tends to be decomposed into pyridinic and quaternary N. Mechanisms of NO, CO and CO2 evolution during TPD are proposed and lattice oxygen is suggested to be an important oxygen resource. Regeneration process indicates that coke-C tends to preferentially oxidise compared with coke-N. Hence, new technology for promoting nitrogen-containing compounds conversion will benefit the in-situ reduction of NO by CO during FCC regeneration. PMID:27270486

  13. Nitrogen Chemistry and Coke Transformation of FCC Coked Catalyst during the Regeneration Process.

    Science.gov (United States)

    Shi, Junjun; Guan, Jianyu; Guo, Dawei; Zhang, Jiushun; France, Liam John; Wang, Lefu; Li, Xuehui

    2016-01-01

    Regeneration of the coked catalyst is an important process of fluid catalytic cracking (FCC) in petroleum refining, however, this process will emit environmentally harmful gases such as nitrogen and carbon oxides. Transformation of N and C containing compounds in industrial FCC coke under thermal decomposition was investigated via TPD and TPO to examine the evolved gaseous species and TGA, NMR and XPS to analyse the residual coke fraction. Two distinct regions of gas evolution are observed during TPD for the first time, and they arise from decomposition of aliphatic carbons and aromatic carbons. Three types of N species, pyrrolic N, pyridinic N and quaternary N are identified in the FCC coke, the former one is unstable and tends to be decomposed into pyridinic and quaternary N. Mechanisms of NO, CO and CO2 evolution during TPD are proposed and lattice oxygen is suggested to be an important oxygen resource. Regeneration process indicates that coke-C tends to preferentially oxidise compared with coke-N. Hence, new technology for promoting nitrogen-containing compounds conversion will benefit the in-situ reduction of NO by CO during FCC regeneration. PMID:27270486

  14. Recycling of hazardous waste materials in the coking process.

    Science.gov (United States)

    Alvarez, R; Barriocanal, C; Díez, M A; Cimadevilla, J L G; Casal, M D; Canga, C S

    2004-03-01

    Every year the coking industry produces a significant amount of tarry and other wastes in byproducts plants. For the most part these wastes have not been put to any practical use. In addition, an integrated factory produces several waste oils which differ in composition and quantity, e.g., wastes from the steel rolling-mill process. In this work, the possibility of using such waste materials as binders in a partial briquetting process for metallurgical coke production is explored. By means of this coking procedure, a strong metallurgical coke not inferior in quality to coke from conventional coal blends is produced at pilot and semi-industrial scales. The use of such wastes, some of which are classified as hazardous materials, will avoid the need for dumping, thereby contributing to the protection of the environment as well as reducing the costs related to waste disposal. PMID:15046368

  15. Disposal of Waste Plastics With Traditional Coking Process

    Institute of Scientific and Technical Information of China (English)

    CAI Jiu-ju; YU Guang-wei; LIAO Hong-qiang; QIAN Kai; ZHAO Pen; HE Ya-bin

    2006-01-01

    A new technology for treating waste plastics (WP) by traditional coking process was introduced. With a thermo-balance and a 10 g atmospheric fixed bed reactor, the thermo-gravimetric behavior and product were studied during co-coking of WP with blended coal. And then, using a coke-oven with capacity of 200 kg, the characteristics of products were assessed. The results showed that there is an overlapping temperature range (200-550 ℃) of decomposition between WP and blended coal, and the pyrolysis synergism index η and synergism strength β proposed could evaluate the synergism between them. 1% of added WP results in the maximum synergism in all series experiments. The increase of added WP decreases the synergism. Tar yield in co-coking is increased with the decrease of water yield for synergism. Moreover, it was also found that the quality indexes of coke, such as M10, M40, CRI and CSR, are degraded with the increase of WP until 4%, though the quality of tar and gas is optimized for WP addition.

  16. Oil sand process-affected water treatment using coke adsorption

    Energy Technology Data Exchange (ETDEWEB)

    Gamal El-Din, M.; Pourrezaei, P.; Chelme-Ayala, P.; Zubot, W. [Alberta Univ., Edmonton, AB (Canada). Dept. of Civil and Environmental Engineering

    2010-07-01

    Oil sands operations generate an array of oil sands process-affected water (OSPW) that will eventually be released to the environment. This water must be evaluated within conventional and advanced water treatment technologies. Water management strategies propose options for increased reuse and recycling of water from settling ponds, as well as safe discharge. This presentation outlined the typical composition of OSPW. Constituents of concern in OSPW include suspended solids, hydrocarbons, salts, ammonia, trace metals, and dissolved organics such as naphthenic acids (NAs). Petroleum coke is one of the by-products generated from bitumen extraction in the oil sands industry and can be used as one of the possible treatment processes for the removal of organic compounds found in OSPW. Activated carbon adsorption is an effective process, able to adsorb organic substances such as oils, radioactive compounds, petroleum hydrocarbons, poly aromatic hydrocarbons and various halogenated compounds. The objectives of this study were to evaluate the production of activated carbon from petroleum coke using steam as the activation media; to determine the factors affecting the absorption of NAs; and to evaluate the activated coke adsorption capacity for the reduction of NAs and dissolved organic carbons present in OSPW. It was concluded that petroleum non-activated coke has the ability to decrease COD, alkalinity, and NA concentration. tabs., figs.

  17. Desulphurizing of coke oven gas by the Stretford process in the San Giuseppe di Cairo coke plant

    Energy Technology Data Exchange (ETDEWEB)

    Borello, G.; Pastorino, L.

    1990-01-01

    The chemistry of the Stretford process and the plant used at this Italian coke works are described. Operating conditions, maintenance needs, overall cost and modifications to overcome problems are discussed.

  18. Application of coke dry quenching technology in the production of the cleaning type heat recovery coke oven%干熄焦技术在清洁型热回收焦炉中的应用

    Institute of Scientific and Technical Information of China (English)

    黄岭

    2011-01-01

    对清洁型热回收焦炉熄焦方式进行了评价,指出干熄焦技术在节能、环保、改善焦炭质量以及经济效益上的积极意义。%By assessing the method of coke quenching technology of the cleaning type heat recovery coke oven,the positive significance of coke dry quenching technology in energy-saving,environmental protection,the quality of coke improving and economic effect was displayed.

  19. Effects of process parameters on selected functions describing coking

    Energy Technology Data Exchange (ETDEWEB)

    Postrzednik, S. (Politechnika Slaska, Gliwice (Poland). Instytut Techniki Cieplnej)

    1987-10-01

    Evaluates a mathematical method for optimization of black coal coking. Mathematical models describe effects of groups of parameters: indices that characterize properties of coal mixtures, parameters that describe technology of coal coking, indices that characterize design and operation of a coke oven. Using the mathematical models, effects of groups of parameters on selected functions that describe coal coking are evaluated. Examples of calculations are discussed. An uncomplicated linear algorithm for optimization of coking is characterized. 6 refs.

  20. Granulation of coke breeze fine for using in the sintering process

    OpenAIRE

    Mohamed F.M.; El-Hussiny N.A.; Shalabi M.E.H.

    2010-01-01

    Coke breeze is the main fuel used in the sintering process. The value of -3+1 mm. represents the most favorable particle size for coke breeze in the sintering process. About 20% of total coke fines (-0.5 mm) are produced during different steps of preparation. Introducing these fines during the sintering process proves to be very harmful for different operating parameters. Thus ,this study aims at investigating the production of granules resulting from these fines using molasses as organ...

  1. Granulation of coke breeze fine for using in the sintering process

    Directory of Open Access Journals (Sweden)

    Mohamed F.M.

    2010-01-01

    Full Text Available Coke breeze is the main fuel used in the sintering process. The value of -3+1 mm. represents the most favorable particle size for coke breeze in the sintering process. About 20% of total coke fines (-0.5 mm are produced during different steps of preparation. Introducing these fines during the sintering process proves to be very harmful for different operating parameters. Thus ,this study aims at investigating the production of granules resulting from these fines using molasses as organic binder and its application in sintering of an iron ore. The results showed that the granules having the highest mechanical properties were obtained with 14.5 wt % molasses addition. The sintering experiments were performed by using coke breeze in different shapes (-3+1 mm in size, coke breeze without sieving and coke breeze granules -3+1 mm. The reduction experiments, microscopic structure and X-ray analysis for the produced sinter were carried out. The results revealed that, all sinter properties (such as shatter test, productivity of sinter machine and blast furnace, reduction time and chemical composition for produced sinter by using coke breeze with size -3+1 mm and coke breeze granules were almost the same. The iron ore sinter which was produced by using coke breeze without sieving yielded low productivity for both sinter machine and blast furnace. Furthermore, using coke breeze without sieving in sintering of an iron ore decreases the vertical velocity of sinter machine and increases the reduction time.

  2. Behaviour of coal associated minerals during coking and blast furnace processes. A review

    Energy Technology Data Exchange (ETDEWEB)

    Gornostayev, Stanislav; Haerkki, Jouko [Lab. of Process Metallurgy, Univ. of Oulu (Finland); Kerkkonen, Olavi [Ruukki Oyj, Raahe (Finland)

    2009-06-15

    Metallurgical coke is made from a mix of several types of coal that contain various minerals, including quartz, carbonates, feldspars, sulphides and a number of phyllosilicates, represented by clay minerals and micas. During coking and coke consumption processes the minerals undergo various physical and chemical changes, which in the case of coke oven batteries include desulphurization, decarbonation, dehydration, dehydroxylation, polymorph transformations, melting with the formation of an alkali and silica-rich liquid, and transformation to another crystalline phase. The typical modifications of mineral phases in a blast furnace (BF) coke are polymorph transformations, melting, and the formation of another crystalline phase. These events are also preceded by notable changes in the shape of crystalline aggregates. All these changes affect the coke properties and the processes occurring in a BF. Mineralogical data can help us to better understand the processes taking place in coke batteries and in a BF, and to improve the quality of a coke by more careful selection of coal blends and setting optimal temperatures for its pre-heating. The degradation of a BF coke by alkalis can be reduced by the addition of certain minerals to the feed coke before charging into the BF. (orig.)

  3. Application of fine-grained coke breeze fractions in the process of iron ore sintering

    Directory of Open Access Journals (Sweden)

    M. Niesler

    2014-01-01

    Full Text Available The testing cycle, described in the paper, included fine-grained coke breeze granulation tests and iron concentrate sintering tests with the use of selected granulate samples. The use of granulated coke breeze in the sintering process results in a higher process efficiency, shorter sintering duration and fuel saving.

  4. Characterization of semi-coke generated by coal-based direct reduction process of siderite

    Institute of Scientific and Technical Information of China (English)

    朱德庆; 罗艳红; 潘建; 周仙霖

    2015-01-01

    Solid wastes derived from metallurgical industries pose a significant threat to environment. The utilization and disposal of these solid wastes are the major concern in the world. Semi-coke generated in coal-based direct reduction process of iron ore is a by-product and its suitable utilization is not available so far. In order to handle it properly, the characteristics of this by-product were comprehensively investigated. A series of analysis methods were used to demonstrate its mineral compositions, petrography and physico-chemical properties. The results reveal that the semi-coke has poor washability. The fixed carbon content of semi-coke reaches 76.11% and the gross calorific value is 28.10 MJ/kg, both of which are similar to those of traditional sinter coke breeze. Also, semi-coke ash possesses lower content of SiO2, Al2O3, S and higher content of CaO and MgO, which could improve the strength of sinter ore when partially substituting for coke breeze in sintering. Semi-coke features well-development porous structure and higher reaction activity, which predicts that the sintering speed could be elevated to some extent when employing it as a partial replacement of coke breeze, so the studies further suggest that the potential adverse effect of the high reactivity on sintering process could be weakened by adequately coarsening the semi-coke’s particle size.

  5. Clean utilization of high sulphur petroleum coke by circulating fluidized bed combustion (CFBC) in Romania

    International Nuclear Information System (INIS)

    The economic and environmental problems caused by inefficient utilization of residual high-sulphur petroleum coke resulted from oil cracking in Romania is discussed. A special research programme applying CFBC technology has been carried out in the Institute for Power Equipment, Bucharest. The results from both laboratory facilities and pilot plant are presented. The main operating conditions and parameters are pointed out. Data on quality and composition of petroleum coke, combustion efficiency, temperature range in different zones and flue gas composition at distinct operating loads are given. The results obtained will be used for innovative design of CFBC boilers based on petroleum coke. A project for implementing a CFBC boiler in one of the Romanian oil refineries is being developed. An analysis of technical and economic advantages of these boilers for energy generation is presented

  6. Identification and removal of polycyclic aromatic hydrocarbons in wastewater treatment processes from coke production plants.

    Science.gov (United States)

    Zhang, Wanhui; Wei, Chaohai; Yan, Bo; Feng, Chunhua; Zhao, Guobao; Lin, Chong; Yuan, Mengyang; Wu, Chaofei; Ren, Yuan; Hu, Yun

    2013-09-01

    Identification and removal of polycyclic aromatic hydrocarbons (PAHs) were investigated at two coke plants located in Shaoguan, Guangdong Province of China. Samples of raw coking wastewaters and wastewaters from subunits of a coke production plant were analyzed using gas chromatography-mass spectrometry (GC/MS) to provide a detailed chemical characterization of PAHs. The identification and characterization of PAH isomers was based on a positive match of mass spectral data of sample peaks with those for PAH isomers in mass spectra databases with electron impact ionization mass spectra and retention times of internal reference compounds. In total, 270 PAH compounds including numerous nitrogen, oxygen, and sulfur heteroatomic derivatives were positively identified for the first time. Quantitative analysis of target PAHs revealed that total PAH concentrations in coking wastewaters were in the range of 98.5 ± 8.9 to 216 ± 20.2 μg/L, with 3-4-ring PAHs as dominant compounds. Calculation of daily PAH output from four plant subunits indicated that PAHs in the coking wastewater came mainly from ammonia stripping wastewater. Coking wastewater treatment processes played an important role in removing PAHs in coking wastewater, successfully removing 92 % of the target compounds. However, 69 weakly polar compounds, including PAH isomers, were still discharged in the final effluent, producing 8.8 ± 2.7 to 31.9 ± 6.8 g/day of PAHs with potential toxicity to environmental waters. The study of coking wastewater herein proposed can be used to better predict improvement of coke production facilities and treatment conditions according to the identification and removal of PAHs in the coke plant as well as to assess risks associated with continuous discharge of these contaminants to receiving waters. PMID:23589270

  7. The effects of the coke addition and the heating time on the efficiency of chlorination process

    International Nuclear Information System (INIS)

    The preparation of mixed pellet, ZrO2, coke and sucrose, for chlorinating process of ZrO2 pellet has been performed. In this experiments the studied parameters were coke addition and the heating time. The addition of coke was 9.72 grams, 10.5 grams and 11 for the mixture of the 87 grams ZrO2 and 3.5 grams sucrose. The purpose of the coke addition is to from ZrC, which is corresponding to Kroll process with carbon-chlor methos. The weight of cokes had been calculated beyond the stoichiometry. The heating times was held in 10 minutes, 15 minutes, and 20 minutes at the temperature of 100oC that was below the evaporation coke temperature of 315oC. The result show that the efficiency of chlorinating of ZrO2 pellet could be reached of 82.16% with the addition of coke mass of 11 grams at the heating temperature of 100oC with the heating time of 20 minutes

  8. The Release of Trace Elements in the Process of Coal Coking

    OpenAIRE

    Jan Konieczyński; Elwira Zajusz-Zubek; Magdalena Jabłońska

    2012-01-01

    In order to assess the penetration of individual trace elements into the air through their release in the coal coking process, it is necessary to determine the loss of these elements by comparing their contents in the charge coal and in coke obtained. The present research covered four coke oven batteries differing in age, technology, and technical equipment. By using mercury analyzer MA-2 and the method of ICP MS As, Be, Cd, Co, Hg, Mn, Ni, Se, Sr, Tl, V, and Zn were determined in samples of ...

  9. The Release of Trace Elements in the Process of Coal Coking

    Directory of Open Access Journals (Sweden)

    Jan Konieczyński

    2012-01-01

    Full Text Available In order to assess the penetration of individual trace elements into the air through their release in the coal coking process, it is necessary to determine the loss of these elements by comparing their contents in the charge coal and in coke obtained. The present research covered four coke oven batteries differing in age, technology, and technical equipment. By using mercury analyzer MA-2 and the method of ICP MS As, Be, Cd, Co, Hg, Mn, Ni, Se, Sr, Tl, V, and Zn were determined in samples of charge coal and yielded coke. Basing on the analyses results, the release coefficients of selected elements were determined. Their values ranged from 0.5 to 94%. High volatility of cadmium, mercury, and thallium was confirmed. The tests have shown that although the results refer to the selected case studies, it may be concluded that the air purity is affected by controlled emission occurring when coke oven batteries are fired by crude coke oven gas. Fugitive emission of the trace elements investigated, occurring due to coke oven leaks and openings, is small and, is not a real threat to the environment except mercury.

  10. Process for converting coal into liquid fuel and metallurgical coke

    Science.gov (United States)

    Wolfe, Richard A.; Im, Chang J.; Wright, Robert E.

    1994-01-01

    A method of recovering coal liquids and producing metallurgical coke utilizes low ash, low sulfur coal as a parent for a coal char formed by pyrolysis with a volatile content of less than 8%. The char is briquetted and heated in an inert gas over a prescribed heat history to yield a high strength briquette with less than 2% volatile content.

  11. Heat Transfer Characteristics of Calcined Petroleum Coke in Waste Heat Recovery Process

    Directory of Open Access Journals (Sweden)

    Bin Zheng

    2016-01-01

    Full Text Available This paper reports the results of heat transfer characteristics of calcined petroleum coke in waste heat recovery process. The model of heat exchanger was set up. The model has been used to investigate the effects of porosity (0.58 to 0.79, equivalent heat conductivity coefficient (0.9 to 1.1, and equivalent specific heat (0.9 to 1.1. The calculated values of calcined petroleum coke temperature showed good agreement with the corresponding available experimental data. The temperature distribution of calcined petroleum coke, the calcined petroleum coke temperature at heat exchanger outlet, the average heat transfer coefficient, and the heat recovery efficiency were studied. It can also be used in deriving much needed data for heat exchanger designs when employed in industry.

  12. Milling Process of Petroleum Coke for Sintered Steel Applications

    OpenAIRE

    Velasco, F.; S. Guzmán; Rabanal, M. E.; Jiménez-Mateos, J. M.; Echeberria, J.; Ayerbe, E.; Calero, J.

    2011-01-01

    The effect of milling on different properties of a petroleum coke has been evaluated. The material was subjected to planetary milling at two different rates (400 and 600 rev min-1) for different times up to 48 h. The milled material was characterised by scanning electron microscopy, X-ray diffraction, sieve analysis, thermal analysis, chemical analysis, specific surface area and compressibility has been undertaken. The results show that the milling produces a very quick loss of the crystal st...

  13. Coke fouling process on the oil refining; Processo de incrustacao por coque no refino do petroleo

    Energy Technology Data Exchange (ETDEWEB)

    Bombardelli, Clovis; Fiorentin, Leila D.; Negrao, Cezar O.R.; Franco, Admilson T. [Centro Federal de Educacao Tecnologica do Parana (CEFET-PR), Curitiba, PR (Brazil). Programa de Pos-Graduacao em Engenharia Mecanica e de Materiais (PPGEM)

    2004-07-01

    The heavy crude fraction processing is performed under very high vacuum to minimize thermal cracking which cause coke deposition and damage the equipment. The current tendency is to process heavier oil leading to higher process temperatures and consequently to greater fouling. This situation demands better knowledge fouling process by carbonization. This problem is pronounced in the residual gasoil region of a vacuum distillation unit because it obstructs the recirculation circuits and the spray system with serious environmental and economics implications. This paper review the main correlated published work related to coke generation and fouling and presents a discussion about the works. (author)

  14. Decomposition of Organic Compounds in Coke Plant Wastewater by Ultrasonic Irradiation and Its Combined Process

    Institute of Scientific and Technical Information of China (English)

    XU Jin-qiu; JIA Jin-ping; WANG Jing-wei

    2004-01-01

    The paper deals with the degradation of the organic compounds in the coke plant wastewater by the combined process of ultrasonic irradiation and activated sludge. The influence factors of the ultrasonic degradation effect such as air atmosphere, initial concentration, ultrasonic power density and the category and consumption of catalyst were investigated. A water quality model was used to explain the degradation of different kinds of organic compounds in the coke plant wastewater by ultrasonic irradiation. After the wastewater was treated by the combined process of ultrasonic irradiation and activated sludge, the COD degradation efficiency was 95. 74 %, which is 63. 49% higher than that by the process of activated sludge alone.

  15. Heat Transfer Characteristics of Calcined Petroleum Coke in Waste Heat Recovery Process

    OpenAIRE

    Bin Zheng; Yongqi Liu; Lichen Zou; Ruiyang Li

    2016-01-01

    This paper reports the results of heat transfer characteristics of calcined petroleum coke in waste heat recovery process. The model of heat exchanger was set up. The model has been used to investigate the effects of porosity (0.58 to 0.79), equivalent heat conductivity coefficient (0.9 to 1.1), and equivalent specific heat (0.9 to 1.1). The calculated values of calcined petroleum coke temperature showed good agreement with the corresponding available experimental data. The temperature distri...

  16. Peculiarities of accumulation of nonstructural carbohydrates in shoots of various species of acer genus in conditions of coke process

    Directory of Open Access Journals (Sweden)

    V. S. Bilchuk

    2005-11-01

    Full Text Available The research results on influence of the by-product-coking industry emission on starch and saccharose accumulation in sprouts of the Acer L. species are presented. The toxic ingredients of the coke production wastes inhibit the process of starch hydrolysis that provokes considerable decrease of the sugars content and negative influence on the plants’ winter hardiness are established.

  17. Experimental study on coke and heavy oil co-conversion process for production of light olefins and synthesis gas

    International Nuclear Information System (INIS)

    A new process, coke and heavy oil co-conversion for production of light olefins (ethylene and propylene) and synthesis gas, was introduced in this paper. Following the technological principle of this process, light olefins and synthesis gas could be produced. Using a fixed bed as the reactor and coke and Shengli atmospheric residue as raw materials in the preliminary study of hot simulative experiments, the effects of operating parameters on the gaseous products components and produced coke were investigated. When the mass ratio of oxygen/steam/residue was set at 0.3/1.0/1.0 and the pyrolysis temperature at 800 oC, while the residence time lasted less than 0.5 s, the contents of light olefins (C2H4, C3H6), alkanes (CH4, C2H6) and synthesis gas (H2, CO) were about 24%, 28% and 37%, respectively. The SEM images of the produced coke on the coked surface medium from residue pyrolysis were observed, and the results showed that the produced coke was almost consumed with blown oxygen. All the results demonstrated that the coke and heavy oil co-conversion process (CHCP) could produce light olefins and synthesis gas together, and the coking problem could be solved effectively. Therefore, the concept of this process is positive and feasible

  18. CO2-pellet cleaning process cuts costs

    International Nuclear Information System (INIS)

    The Non Destructive Cleaning (NDC) process is truly a ''dry process'' that generates no secondary waste streams. Since no solid grit or aggregate is used, there is no need for bulk radioactive solid waste handling equipment. Moreover, since no chemicals are used, the mobile decontamination facility requires no radioactive chemical processing or mixed waste handling facilities. Instead the NDC process uses solid carbon dioxide particles propelled by dry compressed air as the cleaning medium. The carbon dioxide particles shatter upon impact with the surface of the material to be cleaned and flash into dry carbon dioxide gas. This flashing into gas results in a rapid volume expansion of about ten to one. The cleaning action is due to the rapidly expanding carbon dioxide gas flashing into the surface of the item to be cleaned (which is porous at the microscopic level) and flushing foreign materials out. The microscopic particles of foreign material are captured on high efficiency particulate filters. Larger sized fragments are lifted off the surface by the flashing carbon dioxide gas, fall to the bottom of the cleaning area and are vacuumed away to dry air filters. The NDC process also has the advantage that it does not attack the surface of the material being cleaned, making it unique among cleaning processes. (author)

  19. China's coke industry: Recent policies, technology shift, and implication for energy and the environment

    International Nuclear Information System (INIS)

    China is the largest coke producer in the world, accounting for over 60% of the world coke production, which makes the coke industry in China a significant coal consumer and air pollutant emitter. Recently, China has taken a series of measures to improve energy efficiency and reduce emissions from the coke industry, including eliminating old and low energy-efficiency coking technologies, promoting advanced technologies, and strengthening energy and environmental requirements on coking processes. As a consequence, China's coke industry is experiencing an unprecedented technology shift, which was characterized by the elimination of old, inefficient, and polluting indigenous ovens and small machinery ones within 10 years. This study examines the policies and the prompt technology shift in China's coke industry, as well as the associated energy and environmental effects, and discusses the implications with respect to the development of the coke industry in China towards a more efficient and clean future. As China sets stricter requirements on energy efficiency and the ambient environment, a more significant change focusing on technologies of energy saving and emission reduction is urgently needed at present. Those mature technologies, including coke dry quenching, coke oven gas recycle, fine particle removal, etc., should be enforced in the near future. - Highlights: ► With 60% of world coke output, China's coke making has big energy/pollution issues. ► Actions were taken to improve energy and environmental performance of coke plants. ► China's coke industry is experiencing an unprecedented technology shift. ► Another shift, focusing on technologies of energy and emission saving, is needed. ► More measurement studies on coking emissions are needed given the importance.

  20. Dale Coke: Coke Farm

    OpenAIRE

    Farmer, Ellen

    2010-01-01

    Dale Coke grew up on an apricot orchard in California’s Santa Clara Valley. In 1976 he bought ten acres of farmland near Watsonville in Santa Cruz County but continued to work repairing fuel injection systems rather than farming at his new home. In 1981, a struggle with cancer inspired him to rethink his life and become an organic farmer. His neighbor, who had grown strawberries using pesticides and chemical fertilizers, asserted that strawberries could not be grown organically. Coke set out ...

  1. Recent Advances in Precombustion Coal Cleaning Processes

    Institute of Scientific and Technical Information of China (English)

    Shiao-HungChiang; DaxinHe

    1994-01-01

    The mineral matter in coal constitutes a major impediment to the direct use of coal in power plants.A concerted effort has been mounted to reduce the ash/sulfur contents in product coal to meet the ever more stringent environmental regulations.In recent years,significant advances have taken place in fine coal cleaning technologies.A review of recent developments in aveanced physical,chemical and biological processes for deep-cleaning of fine coal is presented.

  2. Chemical cleaning processes - present and future

    International Nuclear Information System (INIS)

    Corrosion products and impurities can accumulate in the secondary side of steam generators causing accelerated corrosion, steam flow disruption and heat transfer loss. Traditionally, chemical cleaning processes have been performed using multi-step processes that employ relatively concentrated reagents (e.g. EPRI-SGOG, 10-20 wt.%), that are applied at elevated temperatures. The use of such reagents dictates the use of large and relatively complex reagent handling systems for both reagent preparation and disposal. The significant duration and cost of each chemical clean has dictated that these cleaning processes are only applied on a remedial basis. An assessment of existing technology was carried out and improvements to the EPRI-SGOG processes are being developed. Results of these assessments are reported. Advanced processes are being developed by Atomic Energy of Canada Limited that use lower concentrations of reagents, require shorter application times and generate lower amounts of waste. This technology can be used on a preventive basis to keep steam generators clean. Included are: A dilute regenerative process that is applied during shutdown. The dilute reagent is continuously recirculated and regenerated during the cleaning process, resulting in shorter application times using modular and portable equipment. The low reagent concentration results in a significantly reduced waste volume. For deposits containing both magnetite and copper a pseudo one-step process (using the same base electrolyte and pH) is used with alternate addition of oxidizing or reducing agents; A dilute on-line process that can be used while the reactor is operating. Such a process would be used on a periodic basis and dislodged oxides removed by blowdown or by mechanical means; Additives that can be used to keep steam generators clean. A demonstration of this technology is currently being planned. Details of these technologies will be described. (author)

  3. New process for producing methanol from coke oven gas by means of CO2 reforming. Comparison with conventional process

    OpenAIRE

    Bermúdez Menéndez, José Miguel; Ferrera Lorenzo, Nuria; Luque, S.; Arenillas de la Puente, Ana; Menéndez Díaz, José Ángel

    2013-01-01

    [EN] A novel method of producing methanol from coke oven gas (COG), involving the CO2 reforming of COG to obtain an appropriate syngas for the synthesis of methanol is proposed. This method is compared with a conventional process of methanol synthesis from natural gas, in terms of energy consumption, CO2 emissions, raw material exploitation and methanol purity. Whereas this new process requires the consumption of less energy, the conventional process allows a higher energy recovery. CO2 emiss...

  4. Alpha Removal Process Filter Cleaning Recommendations

    International Nuclear Information System (INIS)

    The Savannah River Site (SRS) is developing a process to treat radioactive waste that is low in cesium-137, but high in strontium-90, plutonium, uranium, and neptunium. Defense Waste Processing Facility (DWPF) personnel asked Savannah River Technology Center (SRTC) personnel to provide recommendations for chemically cleaning the Alpha Removal Process filters. The authors reviewed previous SRTC filter cleaning experience with bench-scale radioactive filters and pilot-scale simulant filters from tests with simulated and actual waste. From reviewing the previous filter cleaning data and assuming the heel in the 512-S filtration system is 85 gallons or less, the authors recommendations and approach to the inquiry are contained in this report

  5. 焦炉顶装改捣固后工艺及焦炭质量对比%Comparison of the process and coke quality for modifying top charging coke oven battery to stamp charging

    Institute of Scientific and Technical Information of China (English)

    马力辉

    2015-01-01

    This paper introduces the change of process and coke quality after modifying the 4. 3m top charging coke oven battery to stamp charging. After the modification, the coke yield has almost remained same as before,while the coke strength at cold and hot conditions has increased,and the coke screening has been improved,the metallurgical coke rate could be increased by 2. 5%,coke nut yield has been reduced by 1. 5%,and coke breeze yield has been reduced by 0. 5%.%介绍了4.3m焦炉顶装改造为捣固生产后工艺和焦炭质量的变化,由顶装改造为捣固生产后,产量基本保持不变,焦炭的冷热态强度提高,焦炭筛分改善,冶金焦率可以提高2.5%,焦丁产率降低1.5%,焦末产率降低0.5%。

  6. Reduction of NO[sub x] emissions coke oven gas combustion process

    Energy Technology Data Exchange (ETDEWEB)

    Terza, R.R. (USS Clairton Works, PA (United States)); Sardesai, U.V. (Westfield Engineering and Services, Inc., Houston, TX (United States))

    1993-01-01

    The paper describes by-product processing at Clairton Works which uses a unique cryogenic technology. Modifications to the desulfurization facility, nitrogen oxide formation in combustion processes (both thermal and fuel NO[sub x]), and the boilers plants are described. Boilers were used to study the contribution of fuel NO[sub x] formation during the combustion of coke oven gas. Results are summarized. The modifications made to the desulfurization facility resulted in the overall H[sub 2]S emission being reduced by 2-4 grains/100scf and the NO[sub x] emission being reduced by 21-42% in the boiler stacks.

  7. Cleaning of process and utility systems

    International Nuclear Information System (INIS)

    The cleaning of the process and utility equipment and systems forms part of the underlying strategy of planning and implementation. General observation shows that planning is the first essential element to a successful project. A prerequisite to good planning is establishing the goals and objectives at the very outset of the Abandonment Planning. These goals and objectives must be measurable against preestablished criteria so that the project can be evaluated to establish the level of success. Good planning can be viewed as a series of hurdles that one must clear to achieve the pre-set goals and objectives. Understanding of the legal, safety, environmental and legislative requirements allows the perimeters and constraints to be established before the final implementation of the, ''CLEANING OF PROCESS AND UTILITY EQUIPMENT AND SYSTEMS'' activities. The very subject of ''CLEANING OF PROCESS AND UTILITY EQUIPMENT AND SYSTEMS'' that may be considered straight forward, because some of these activities often form part of the normal platform operations performed from time to time on these systems. Before implementation of these activities, there must be an understanding of the ground rules and terminology used together with the resultant implications. A question that demonstrates the inherent problems, what does the term ''Clean'' mean? A limited list has been compiled to give some examples of what the dictionary defines the term clean to be; NOT DIRTY; UN-POLLUTED; DECONTAMINATED; STAINLESS; UNCONTAMINATED; SPOTLESS; VIRGIN; UNSTAINED; UNADULTERATED; STERILE; Liaison with Government departments during recent planning activities established a consensus for understanding the term ''Clean'' so that unreasonable expectation with regards to the level of cleanliness would not be greater than that which is practicable

  8. Increasing Liquid Yield and Diesel Fraction in Delayed Coking Process: Mechanism of Liquid Formation

    Institute of Scientific and Technical Information of China (English)

    Mominou Nchare; Shen Benxian; Xu Jiaoliang

    2007-01-01

    The thermal upgrading of two residual oils with different characteristics was studied in a laboratory-scale continuous delayed coking unit.The goal was to investigate the influence of the process variables such as temperature,reaction time and additive on liquid yield and products distribution.A maximum liquid yield of 73% was achieved compared to 69% with the commercial unit.This yield was even increased to 75% under the effect of an additive.The fractionation of liquid oil by simulated vacuum distillation showed a high yield of diesel(46.9%).compared to 28% for the commercial unit.

  9. Study on treatment of coking wastewater by biofilm reactors combined with zero-valent iron process

    International Nuclear Information System (INIS)

    Experiments were conducted to investigate the behavior of the integrated system with biofilm reactors and zero-valent iron (ZVI) process for coking wastewater treatment. Particular attention was paid to the performance of the integrated system for removal of organic and inorganic nitrogen compounds. Maximal removal efficiencies of chemical oxygen demand (COD), ammonia nitrogen (NH3-N) and total inorganic nitrogen (TIN) were up to 96.1, 99.2 and 92.3%, respectively. Moreover, it was found that some phenolic compounds were effectively removed. The refractory organic compounds were primarily removed in ZVI process of the integrated system. These compounds, with molecular weights either ranged 10,000-30,000 Da or 0-2000 Da, were mainly the humic acid (HA) and hydrophilic (HyI) compounds. Oxidation-reduction and coagulation were the main removal mechanisms in ZVI process, which could enhance the biodegradability of the system effluent. Furthermore, the integrated system showed a rapid recovery performance against the sudden loading shock and remained high efficiencies for pollutants removal. Overall, the integrated system was proved feasible for coking wastewater treatment in practical applications

  10. Model predictive control for improving waste heat recovery in coke dry quenching processes

    International Nuclear Information System (INIS)

    CDQ (coke dry quenching) is a widely used method for recovering waste heat in the steel industry. We have developed a novel, data driven modeling approach and model based control for a CDQ unit to increase steam generation in a cogeneration system. First, the correlation between steam generation and TCGB (the temperature of circulation gas entering the associated boiler) was confirmed. Subsequently, a nonlinear variable selection method was employed to build models of TCGB and the carbon monoxide concentration of the circulation gas. The models obtained were implemented to achieve MPC (model predictive control) for regulating the supplementary gas to maximize steam generation in an existing steelmaking plant. Upon comparison of the original process and the proposed modified operation, the effectiveness of the implementation of MPC was justified. The results showed that steam generation was increased by 7%. In our approach, the large amount of available operational data stored electronically was used to establish the models. Modification of the established system is not required. Taking into account that no capital investment is required, the process improvement is remarkable in terms of its return on investment. - Highlights: • This is the first implementation of MPC for the coke dry quenching process. • Correlation between steam generation and circulation gas temperature was verified. • A nonlinear variable selection method was developed to construct the model. • The proposed approach was implemented in an existing steelmaking plant. • The results show that the steam generation increases by 7%

  11. Mild coal extraction for the production of anode coke from Blue Gem coal

    Energy Technology Data Exchange (ETDEWEB)

    Rodney J. Andrews; Terry Rantell; David Jacques; James C. Hower; J. Steven Gardner; Mike Amick [University of Kentucky, Lexington, KY (United States). Center for Applied Energy Research

    2010-09-15

    The quality and availability of petroleum coke used in the manufacture of carbon anodes for aluminum production is a growing concern to the industry. Coke quality and yields have progressively declined as changes in refinery practice and the move towards processing an increasing proportion of heavier sour crudes have affected coke properties, resulting in an increase in the metal impurities and sulfur content of the coke. An alternative supply of anode coke is required to supplement or eventually replace calcined petroleum coke. The significant domestic reserves of coal could represent a viable carbon resource for anode production, provided defined coke specifications can be met and at a cost that is economically viable. The principal objective of this study was to examine the feasibility of producing anode grade coke by the UKCAER process for the mild solvent extraction of coal. Blue Gem coal from Eastern Kentucky was dissolved in a high boiling point solvent, the mineral matter and unreacted products removed by filtration, and the clean coal liquid converted to coke. The performance of the coal in solvent extraction was compared to a very reactive coal from Western Kentucky. A simple solvent-extraction screening test was established to assess potential candidate materials and process variables without the need for prolonged and complex routines. The coals were assessed in more detail to determine the optimum process conditions by conducting larger scale extraction tests to yield sufficient material for conversion to coke. The green cokes were calcined and the products characterized. The composition and structure of the calcined cokes were compared to typical petroleum coke and assessed for their use in the fabrication of carbon anodes. 21 refs., 11 figs., 4 tabs.

  12. Coal Beneficiation Technology for Coking & Non-Coking Coal Meant For Steel and Thermal Power Plants

    OpenAIRE

    Manoj Kumar Sharma; Gohil Priyank; Nikita Sharma

    2015-01-01

    There are 21 coking coal washeries in production both in private and public sectors. Production of clean coal in these washeries during 1989-90 was 12 million tonne and it is expected to go up to 37 million, tonne during 2015-16. Planning Commission has taken the decision that non-coking coal meant for Thermal Power Plants situated far away from feeding coalfield, should be beneficiated. Coal Washing is a process of separation mainly based on difference in Specific Gravity of Coal and associa...

  13. New Coke Oven Facilities at Linhuan Coal Chemical Company Adopt LyondellBasell's Aromatics Extraction Process

    Institute of Scientific and Technical Information of China (English)

    2008-01-01

    @@ The new 80 kt/a coal chemical unit at the Linhuan Coal Chemical Company in Anhui province will adopt the aro-matics extraction process licensed by LyondellBasell Company. This unit is expected to come on stream by 2009.This technology is suitable for manufacture of high-purity aromatics with broad adaptability and large scale produc-tion capability. In the previous year LyondellBasell was awarded six patents on aromatics extraction process. It is told that the achievements to be adopted by the Linhuan Coal Chemical Company are partly a series of aromatics extrac-tion processes for recovery of coke oven light oil performed by LyondellBasell.

  14. The adsorption of oil sands naphthenic acids from process-affected tailings water using activated petroleum coke

    Energy Technology Data Exchange (ETDEWEB)

    Small, C.C.; Hashisho, Z.; Ulrich, A.C. [Alberta Univ., Edmonton, AB (Canada). Dept. of Civil and Environmental Engineering

    2010-07-01

    Eighty percent of the organic acids in the Athabasca oil sands region are comprised of naphthenic acids that are toxic to a variety of aquatic life-forms as well as being highly corrosive. This PowerPoint presentation discussed a method of adsorbing naphthenic acids from process-affected water. Activated petroleum coke was studied in order to investigate optimal physical activation conditions for adsorbing oil sands naphthenic acids. Experimental tests were conducted in a centrifuge and analyzed with Fourier transform infrared (FTIR) spectrometry, scanning electron microscopy (SEM) and fluorescence spectrometry. The study demonstrated that delayed and fluid petroleum cokes can be turned into high surface area carbons with increased activation time, temperature, and steam rate. The coke can be used as an adsorbent to remove oil sands naphthenic acids. tabs., figs.

  15. Combustion Simulation and Quick-freeze Observation of a Cupola-furnace Process Using a Bio-coke Fuel Based on Tea Scum

    Science.gov (United States)

    Ishii, Kazuyoshi; Murata, Hirotoshi; Kuwana, Kazunori; Mizuno, Satoru; Morita, Akihiro; Ida, Tamio

    Global environment problems have become more and more serious in recent years, and reduction of greenhouse gas emission based on Kyoto Protocol adopted at the 3rd conference of the parties of the United nations Framework Convention on Climate Change (COP3); securement of primary energy source and development of clean and renewable energy sources have been pressingly needed in consideration of the predicted depletion of fossil fuel in the future. In this study, we explore the use of a solidified biomass-derived fuel, having the maximum compressive strength of 100MPa and calorific value of 21MJ/kg, in iron-casting or iron-making processes as an alternative fuel to be mixed with coal coke. This study, carried out for internal observation using a quick-freeze technique, observed an actual working cupola furnace under the 20% alternative coal coke operation condition. After quick freeze of the cupola furnace, the solidified biomass fuel was found to inhabit near the iron-melting zone. Especially, this solidified biomass fuel smoothly changes carbonized fuel through high-density state during the operating process. On the other hand, this study tried to simulate gasification combustion under a high temperature environment instead of actual internal combustion of solidified biomass fuel. These combustion mechanisms were confirmed to be similar to diffusion-flame phenomena in general.

  16. Petroleum coke adsorption as a water management option for oil sands process-affected water

    International Nuclear Information System (INIS)

    Water is integral to both operational and environmental aspects of the oil sands industry. A water treatment option based on the use of petroleum coke (PC), a by-product of bitumen upgrading, was examined as an opportunity to reduce site oil sands process-affected water (OSPW) inventories and net raw water demand. Changes in OSPW quality when treated with PC included increments in pH levels and concentrations of vanadium, molybdenum, and sulphate. Constituents that decreased in concentration after PC adsorption included total acid-extractable organics (TAO), bicarbonate, calcium, barium, magnesium, and strontium. Changes in naphthenic acids (NAs) speciation were observed after PC adsorption. A battery of bioassays was used to measure the OSPW toxicity. The results indicated that untreated OSPW was toxic towards Vibrio fischeri and rainbow trout. However, OSPW treated with PC at appropriate dosages was not acutely toxic towards these test organisms. Removal of TAO was found to be an adsorption process, fitting the Langmuir and Langmuir–Freundlich isotherm models. For TAO concentrations of 60 mg/L, adsorption capacities ranged between 0.1 and 0.46 mg/g. This study demonstrates that freshly produced PC from fluid cokers provides an effective treatment of OSPW in terms of key constituents' removal and toxicity reduction. - Highlights: ► Treatment of oil sands process-affected water (OSPW) using petroleum coke (PC) adsorption was investigated. ► PC was effective at adsorbing naphthenic acids with higher cyclicity. ► OSPW treated with PC at appropriate dosages was not toxic towards Vibrio fisheri and rainbow trout. ► The adsorption of organic acids fitted the Langmuir and Langmuir–Freundlich isotherm models. ► PC has the potential to be an effective adsorbent to treat OSPW either directly or as a pretreatment step.

  17. Petroleum coke adsorption as a water management option for oil sands process-affected water

    Energy Technology Data Exchange (ETDEWEB)

    Zubot, Warren [Syncrude Canada Ltd., Research and Development, Edmonton, Alberta, Canada T6N 1H4 (Canada); MacKinnon, Michael D. [OSPM Solutions Ltd., Hamilton, Ontario, Canada L8H 6X2 (Canada); Chelme-Ayala, Pamela; Smith, Daniel W. [University of Alberta, Department of Civil and Environmental Engineering, Edmonton, Alberta, Canada T6G 2W2 (Canada); Gamal El-Din, Mohamed, E-mail: mgamalel-din@ualberta.ca [University of Alberta, Department of Civil and Environmental Engineering, Edmonton, Alberta, Canada T6G 2W2 (Canada)

    2012-06-15

    Water is integral to both operational and environmental aspects of the oil sands industry. A water treatment option based on the use of petroleum coke (PC), a by-product of bitumen upgrading, was examined as an opportunity to reduce site oil sands process-affected water (OSPW) inventories and net raw water demand. Changes in OSPW quality when treated with PC included increments in pH levels and concentrations of vanadium, molybdenum, and sulphate. Constituents that decreased in concentration after PC adsorption included total acid-extractable organics (TAO), bicarbonate, calcium, barium, magnesium, and strontium. Changes in naphthenic acids (NAs) speciation were observed after PC adsorption. A battery of bioassays was used to measure the OSPW toxicity. The results indicated that untreated OSPW was toxic towards Vibrio fischeri and rainbow trout. However, OSPW treated with PC at appropriate dosages was not acutely toxic towards these test organisms. Removal of TAO was found to be an adsorption process, fitting the Langmuir and Langmuir-Freundlich isotherm models. For TAO concentrations of 60 mg/L, adsorption capacities ranged between 0.1 and 0.46 mg/g. This study demonstrates that freshly produced PC from fluid cokers provides an effective treatment of OSPW in terms of key constituents' removal and toxicity reduction. - Highlights: Black-Right-Pointing-Pointer Treatment of oil sands process-affected water (OSPW) using petroleum coke (PC) adsorption was investigated. Black-Right-Pointing-Pointer PC was effective at adsorbing naphthenic acids with higher cyclicity. Black-Right-Pointing-Pointer OSPW treated with PC at appropriate dosages was not toxic towards Vibrio fisheri and rainbow trout. Black-Right-Pointing-Pointer The adsorption of organic acids fitted the Langmuir and Langmuir-Freundlich isotherm models. Black-Right-Pointing-Pointer PC has the potential to be an effective adsorbent to treat OSPW either directly or as a pretreatment step.

  18. Dilute chemical cleaning of PWR steam generators off-line cleaning process evaluation

    International Nuclear Information System (INIS)

    This project evaluated the feasibility of using a low-concentration (approx. 0.5 wt %) chemical cleaning process to remove corrosion product deposits from steam generator surfaces and magnetite from tube-to-support plate crevices of PWR steam generators. The primary objective was to develop a dilute process that could be safely applied at scheduled intervals, such as during normal refueling outages, to maintain a clean operating condition in the steam generator. The dilute chemical cleaning process developed in this project was demonstrated successfully on two model generators which were operated on faulted chemistry by DOE/CRC at Commonwealth's State Line Facility. Unit 5 was cleaned after 48 days of operation with 1% seawater fouling, and Unit 6 was cleaned after 112 days of operations with Lake Michigan water. This report describes work leading to the model generator cleaning demonstrations and provides details of the cleaning operation for each model steam generator

  19. Solid fuels: Analysis of coking process. Feste Brennstoffe: analyse des Entgasungsprozesses; Anwendung des Einflussfaktoren-Prozess-funktionen-Algorithmus

    Energy Technology Data Exchange (ETDEWEB)

    Postrzednik, S. (Politechniki Slaskiej, Gliwice (Poland). Instytut Techniki Ciepinej)

    1991-05-01

    Mathematical models have been useful in the optimisation and control of processes. Coking is a common process for treating solid fuels. A simplification of the calculations is desirable for practical problems, however, without forfeiting the reliability of a complex model. In the present case the parameters of the process for solid fuels were divided into two groups. The reciprocal relations of these parmaeters were evaluated by means of a linear algorithm. 11 refs., 4 figs., 1 tab.

  20. Effects of atamp-charging coke making on strength and high temperature thermal properties of coke.

    Science.gov (United States)

    Zhang, Yaru; Bai, Jinfeng; Xu, Jun; Zhong, Xiangyun; Zhao, Zhenning; Liu, Hongchun

    2013-12-01

    The stamp-charging coke making process has some advantages of improving the operation environment, decreasing fugitive emission, higher gas collection efficiency as well as less environmental pollution. This article describes the different structure strength and high temperature thermal properties of 4 different types of coke manufactured using a conventional coking process and the stamp-charging coke making process. The 4 kinds of cokes were prepared from the mixture of five feed coals blended by the petrography blending method. The results showed that the structure strength indices of coke prepared using the stamp-charging coke method increase sharply. In contrast with conventional coking process, the stamp-charging process improved the coke strength after reaction but had little impact on the coke reactivity index. PMID:25078828

  1. Centralized coke gasification study

    Energy Technology Data Exchange (ETDEWEB)

    du Plessis, Duke [Alberta Innovates (Canada); Pietrusik, Debbie [Alberta Finance and Enterprise (Canada)

    2011-07-01

    By the year 2020 Alberta will produce 3 million barrels of bitumen per day. Refining bitumen yields several by-products such as petroleum coke and off-gasses. These products can be further utilized as a low cost feedstock for additional applications to increase revenue. Alberta currently has the largest amount of coke stockpiled in the world. The presentation explores what is the most profitable way to use this coke and what future technologies would improve the economic and environmental impact of the process. The development of methane and hydrogen becomes competitive at intermediate gas and oil prices. The next generation of gasification technologies is going to be cheaper, efficient and much smaller. Pilot projects have shown positive results. Economies of scale can be reached simply by only 20-30% of annual coke production. The high cost of the current technology is creating the biggest challenge but new technologies and process innovations have the potential to drive down cost.

  2. Performance of batch vacuum distillation process with promoters on coke-plant wastewater treatment

    Energy Technology Data Exchange (ETDEWEB)

    Wei Mao; Hongzhu Ma; Bo Wang [Shaanxi Normal University, Xi' an (China). Institute of Energy Chemistry

    2010-05-15

    This paper presents a simple study of laboratory-scale vacuum distillation process with promoters (VD{sub P}) on coke-plant wastewater, which has the advantage that the chemical reaction and pollutants separation can be concurrent in one pot. The main parameters that evaluate the efficiency of VD{sub P} are conductivity, chemical oxygen demand (COD) and ammonia nitrogen compounds (NH{sub 3}-N). The blank experiment, vacuum distillation (VD) process was also investigated for comparison. The effects of some operating factors, such as, vacuum degree of system, the temperature of wastewater and temperature gradient ({Delta}T) on the treatment efficiency were investigated in detail. And satisfactory results were obtained in the VDP system with caustic soda and slaked lime as promoters. It was found that high COD removal of 99.7% can be obtained in 180 min for caustic soda promoted system (the detailed condition: NaOH 2.0 g, vacuum degree -85 kPa, {Delta}T 11{sup o}C). Meanwhile, near 100% NH{sub 3}-N removal can be obtained simultaneously in this VD{sub P} process.

  3. Coking wastewater treatment for industrial reuse purpose: combining biological processes with ultrafiltration, nanofiltration and reverse osmosis.

    Science.gov (United States)

    Jin, Xuewen; Li, Enchao; Lu, Shuguang; Qiu, Zhaofu; Sui, Qian

    2013-08-01

    A full-scale plant using anaerobic, anoxic and oxic processes (A1/A2/O), along with a pilot-scale membrane bioreactor (MBR), nanofiltration (NF) and reverse osmosis (RO) integrated system developed by Shanghai Baosteel Chemical Co. Ltd., was investigated to treat coking wastewater for industrial reuse over a period of one year. The removals reached 82.5% (COD), 89.6% (BOD), 99.8% (ammonium nitrogen), 99.9% (phenol), 44.6% (total cyanide (T-CN)), 99.7% (thiocyanide (SCN-)) and 8.9% (fluoride), during the A1/A2/O biological treatment stage, and all parameters were further reduced by over 96.0%, except for fluoride (86.4%), in the final discharge effluent from the currently operating plant. The pilot-scale MBR process reduced the turbidity to less than 0.65 NTU, and most of the toxic organic compounds were degraded or intercepted by the A1/A2/O followed MBR processes. In addition, parameters including COD, T-CN, total nitrogen, fluoride, chloride ion, hardness and conductivity were significantly reduced by the NF-RO system to a level suitable for industrial reuse, with a total water production ratio of 70.7%. However, the concentrates from the NF and RO units were highly polluted and should be disposed of properly or further treated before being discharged. PMID:24520694

  4. Functionalization of Petroleum Coke-Derived Carbon for Synergistically Enhanced Capacitive Performance

    OpenAIRE

    Zhang, Yan; Li, Xuejin; Huang, Jufeng; Xing, Wei; Yan, Zifeng

    2016-01-01

    Petroleum coke is a valuable and potential source for clean energy storage if it could be modified legitimately and facilely. In the present study, porous carbon with high surface area and abundant oxygen-containing groups was prepared from petroleum coke by chemical activation and modification processes. The as-prepared carbon exhibits a high surface area (1129 m2 · g−1) and stable micrographic structure. It presents a high specific capacitance and excellent rate performance in KOH electroly...

  5. Petroleum coke adsorption as a water management option for oil sands process-affected water.

    Science.gov (United States)

    Zubot, Warren; MacKinnon, Michael D; Chelme-Ayala, Pamela; Smith, Daniel W; Gamal El-Din, Mohamed

    2012-06-15

    Water is integral to both operational and environmental aspects of the oil sands industry. A water treatment option based on the use of petroleum coke (PC), a by-product of bitumen upgrading, was examined as an opportunity to reduce site oil sands process-affected water (OSPW) inventories and net raw water demand. Changes in OSPW quality when treated with PC included increments in pH levels and concentrations of vanadium, molybdenum, and sulphate. Constituents that decreased in concentration after PC adsorption included total acid-extractable organics (TAO), bicarbonate, calcium, barium, magnesium, and strontium. Changes in naphthenic acids (NAs) speciation were observed after PC adsorption. A battery of bioassays was used to measure the OSPW toxicity. The results indicated that untreated OSPW was toxic towards Vibrio fischeri and rainbow trout. However, OSPW treated with PC at appropriate dosages was not acutely toxic towards these test organisms. Removal of TAO was found to be an adsorption process, fitting the Langmuir and Langmuir-Freundlich isotherm models. For TAO concentrations of 60 mg/L, adsorption capacities ranged between 0.1 and 0.46 mg/g. This study demonstrates that freshly produced PC from fluid cokers provides an effective treatment of OSPW in terms of key constituents' removal and toxicity reduction. PMID:22575375

  6. Development and Testing of the Advanced CHP System Utilizing the Off-Gas from the Innovative Green Coke Calcining Process in Fluidized Bed

    Energy Technology Data Exchange (ETDEWEB)

    Chudnovsky, Yaroslav; Kozlov, Aleksandr

    2013-08-15

    Green petroleum coke (GPC) is an oil refining byproduct that can be used directly as a solid fuel or as a feedstock for the production of calcined petroleum coke. GPC contains a high amount of volatiles and sulfur. During the calcination process, the GPC is heated to remove the volatiles and sulfur to produce purified calcined coke, which is used in the production of graphite, electrodes, metal carburizers, and other carbon products. Currently, more than 80% of calcined coke is produced in rotary kilns or rotary hearth furnaces. These technologies provide partial heat utilization of the calcined coke to increase efficiency of the calcination process, but they also share some operating disadvantages. However, coke calcination in an electrothermal fluidized bed (EFB) opens up a number of potential benefits for the production enhancement, while reducing the capital and operating costs. The increased usage of heavy crude oil in recent years has resulted in higher sulfur content in green coke produced by oil refinery process, which requires a significant increase in the calcinations temperature and in residence time. The calorific value of the process off-gas is quite substantial and can be effectively utilized as an “opportunity fuel” for combined heat and power (CHP) production to complement the energy demand. Heat recovered from the product cooling can also contribute to the overall economics of the calcination process. Preliminary estimates indicated the decrease in energy consumption by 35-50% as well as a proportional decrease in greenhouse gas emissions. As such, the efficiency improvement of the coke calcinations systems is attracting close attention of the researchers and engineers throughout the world. The developed technology is intended to accomplish the following objectives: - Reduce the energy and carbon intensity of the calcined coke production process. - Increase utilization of opportunity fuels such as industrial waste off-gas from the novel

  7. The triumphs of coke

    Energy Technology Data Exchange (ETDEWEB)

    Mott, R.A.

    2004-07-01

    This is a reproduction of a booklet specially written by Dr R.A. Mott and designed by Mr G.E. Hall to mark the jubilee of the Coke Oven Managers' Association, founded in 1915. Whilst mentioning early methods of making coke in Great Britain, it deals particularly with the many developments in coke usage which took place before 1915 and is complementary to the 'History of coke making' written by Dr Mott in 1936. Uses covered include: for malting, for non-ferrous metal making, in an iron blast furnace, in crucible steel making, in the chafery and puddling process, in a foundry cupola, and in railway locomotives. 15 ills.

  8. Limitations of the removal of cyanide from coking wastewater by ozonation and by the hydrogen peroxide-ozone process.

    Science.gov (United States)

    Pueyo, N; Miguel, N; Ovelleiro, J L; Ormad, M P

    2016-01-01

    The purpose of this study is to compare the efficiency of ozonation and the hydrogen peroxide-ozone process for the removal of cyanide from coking wastewater. The most efficient oxidation process is combined with coagulation-flocculation-decantation and lime-soda ash softening pretreatments. The oxidation in aqueous solution and industrial wastewater (at pH 9.5-12.3) by O3 was carried out using a range of concentration of consumed O3 from 10 to 290 mg/L. A molar ratio of H2O2/O3 from 0.1 to 5.2 with different concentrations of O3 constants was used for the H2O2-O3 process. The maximum cyanide removal obtained in coking wastewater was 90% using a mass ratio of O3/CN(-) of 9.5. Using lower concentrations of O3, cyanide is not removed and can even be generated due to the presence of other cyanide precursor organic micropollutants in the industrial matrix. The concentration of O3 is reduced to half for the same cyanide removal efficiency if the pretreatments are applied to reduce the carbonate and bicarbonate ions. The cyanide removal efficiency in coking wastewater is not improved if the O3 is combined with the H2O2. However, the preliminary cyanide removal treatment in aqueous solution showed an increase in the cyanide removal efficiency for the H2O2-O3 process. PMID:27438254

  9. Charging trolley for coke oven. Beskikingsvogn for koksovn

    Energy Technology Data Exchange (ETDEWEB)

    Gregor, K.; Feldhaus, K.

    1984-06-04

    The patent application describes a charging trolley for coke ovens. The trolley has a cover raising device which may be moved along a vertical track in order to raise covers for the oven sharge openings. At the coking process considerable amounts of combustion and coke gases are liberated. They contain large amounts of pollutants such as dust, finely devided solids and various other components. The pollutants settle on the convers and at the openings which leads to less satisfactory stopping and a leak of gases containing such pollutants to the surroundings. In order to avoid or at least reduce considerably such leaks in a simple and reliable way and with little loss of time, a cover cleaning device is constructed. It has at least 2 cleaning segments equipped with cleaning devices wich may move between a position swung away from and one covering the motion track. By help of the cleaning device it is possible to clean the stopper sheets on the covers without disturbing the operation. As a result the opening stoppers are improved and undesired pollution is considerably reduced. The claims concern the design of the charge trolley and the covering and cleaning devices in particular. 4 drawings.

  10. Thermodynamic analysis for a regenerative gas turbine cycle in coking process

    Directory of Open Access Journals (Sweden)

    Zelong Zhang, Lingen Chen, Yanlin Ge, Fengrui Sun

    2014-01-01

    Full Text Available A regenerative gas turbine cycle driven by residual coke oven gas is proposed in this paper. The thermal efficiency and the work output (per ton of coke of the system are analyzed based on thermodynamics and the theory of gas turbine cycle. The influences of the gas release rate, the residual gas rate and the effectiveness of regenerator on the performance of the cycle are analyzed by using numerical examples. It is found that the work output increases with the increase of the residual gas rate while decreases with the increase of the gas release rate. The cycle with regenerator can reach higher thermal efficiency and bigger work output, which means that the coke oven gas is used more effectively. Moreover, there exist two optimal pressure ratios of compressor which lead the maximum thermal efficiency and the maximum specific work, respectively.

  11. An experimental and numerical study of water jet cleaning process

    OpenAIRE

    Guha, Anirban; Barron, Ronald M.; Balachandar, Ram

    2010-01-01

    In this paper, we have experimentally, numerically and theoretically investigated the water jet cleaning process. Very high speed water jets (~80-200 m/s) are typically used in such cleaning operations. These jets diffuse in the surrounding atmosphere by the process of air entrainment and this contributes to the spreading of the jet and subsequent decay of pressure. Estimation of this pressure decay and subsequent placement of the cleaning object is of paramount importance in manufacturing an...

  12. Cleaning Process Development for Metallic Additively Manufactured Parts

    Science.gov (United States)

    Tramel, Terri L.; Welker, Roger; Lowery, Niki; Mitchell, Mark

    2014-01-01

    Additive Manufacturing of metallic components for aerospace applications offers many advantages over traditional manufacturing techniques. As a new technology, many aspects of its widespread utilization remain open to investigation. Among these are the cleaning processes that can be used for post finishing of parts and measurements to verify effectiveness of the cleaning processes. Many cleaning and drying processes and measurement methods that have been used for parts manufactured using conventional techniques are candidates that may be considered for cleaning and verification of additively manufactured parts. Among these are vapor degreasing, ultrasonic immersion and spray cleaning, followed by hot air drying, vacuum baking and solvent displacement drying. Differences in porosity, density, and surface finish of additively manufactured versus conventionally manufactured parts may introduce new considerations in the selection of cleaning and drying processes or the method used to verify their effectiveness. This presentation will review the relative strengths and weaknesses of different candidate cleaning and drying processes as they may apply to additively manufactured metal parts for aerospace applications. An ultrasonic cleaning technique for exploring the cleanability of parts will be presented along with an example using additively manufactured Inconel 718 test specimens to illustrate its use. The data analysis shows that this ultrasonic cleaning approach results in a well-behaved ultrasonic cleaning/extraction behavior. That is, it does not show signs of accelerated cavitation erosion of the base material, which was later confirmed by neutron imaging. In addition, the analysis indicated that complete cleaning would be achieved by ultrasonic immersion cleaning at approximately 5 minutes, which was verified by subsequent cleaning of additional parts.

  13. Thermodynamic analysis for a regenerative gas turbine cycle in coking process

    OpenAIRE

    Zelong Zhang, Lingen Chen, Fengrui Sun

    2014-01-01

    A regenerative gas turbine cycle driven by residual coke oven gas is proposed in this paper. The thermal efficiency and the work output (per ton of coke) of the system are analyzed based on thermodynamics and the theory of gas turbine cycle. The influences of the gas release rate, the residual gas rate and the effectiveness of regenerator on the performance of the cycle are analyzed by using numerical examples. It is found that the work output increases with the increase of the residual gas r...

  14. The mechanism of coking pressure generation I: Effect of high volatile matter coking coal, semi-anthracite and coke breeze on coking pressure and plastic coal layer permeability

    Energy Technology Data Exchange (ETDEWEB)

    Seiji Nomura; Merrick Mahoney; Koichi Fukuda; Kenji Kato; Anthony Le Bas; Sid McGuire [Nippon Steel Corporation, Chiba (Japan). Environment and Process Technology Center

    2010-07-15

    One of the most important aspects of the cokemaking process is to control and restrain the coking pressure since excessive coking pressure tends to lead to operational problems and oven wall damage. Therefore, in order to understand the mechanism of coking pressure generation, the permeability of the plastic coal layer and the coking pressure for the same single coal and the same blended coal were measured and the relationship between them was investigated. Then the 'inert' (pressure modifier) effect of organic additives such as high volatile matter coking coal, semi-anthracite and coke breeze was studied. The coking pressure peak for box charging with more uniform bulk density distribution was higher than that for top charging. It was found that the coking pressure peaks measured at different institutions (NSC and BHPBilliton) by box charging are nearly the same. The addition of high volatile matter coking coal, semi-anthracite and coke breeze to a low volatile matter, high coking pressure coal greatly increased the plastic layer permeability in laboratory experiments and correspondingly decreased the coking pressure. It was found that, high volatile matter coking coal decreases the coking pressure more than semi-anthracite at the same plastic coal layer permeability, which indicates that the coking pressure depends not only on plastic coal layer permeability but also on other factors. Coking pressure is also affected by the contraction behavior of the coke layer near the oven walls and a large contraction decreases the coal bulk density in the oven center and hence the internal gas pressure in the plastic layer. The effect of contraction on coking pressure needs to be investigated further. 33 refs., 18 figs., 5 tabs.

  15. Application of microorganisms in coal cleaning processes

    International Nuclear Information System (INIS)

    A secure energy supply is one of the basic pre-requisites for a sound economic system, sustained standard and quality of life and eventually for the social well-being of each individual. For a progressive country like Pakistan, it is obligatory that all energy options must be pursued vigorously including coal utilization, which given the relatively large resources available, is considered to be one of the major options for the next few hundred years. Bioprocessing of coal in an emerging technology which has started to receive considerable research attention. Recent research activities involving coal cleaning, direct coal conversion, and indirect conversion of coal-derived materials have generated a plethora of facts regarding biochemistry, chemistry, and thermodynamic behavior of coal, in that its bioprocessing is on the verge of becoming and acceptable means to great coals. In this research report, investigations pertaining to the various aspects of coal bio processing, including desulfurization and depyritization are discussed. Bituminous coals varying in total sulfur contents of 3-6% were depyritized more than 90% by mesophilic acidophiles like Thiobacillus ferroxidans and Thiobacillus thio oxidans and thermophilic Sulfolobus brierleyi. The archaebacterium, Sulfolobus brierleyi was found to desulfurize inorganic and organic sulfur components of the coal. Conditions were established under which it can remove more than 30% of the organic sulfur present in the coals. Heterotrophic microorganisms including oxenic and soil isolates were also employed for studying sulfurization. A soil isolate, Oil-2, was found to remove more than 70% dibenzothiophenic sulfur present in an oil-water emulsion (1:20 ratio). Pseudomonas putida and the bacterium oil-2 also remove 60-70% organic sulfur present in the shale-oil. Preliminary results indicate the presence of putatively known Kodama's pathway in the oil-2. The mass balance for sulfate indicated the possibility of the presence

  16. Brief Introduction to Research of Coking with Briquette Blending Process%配型煤炼焦工艺研究概况

    Institute of Scientific and Technical Information of China (English)

    狄红旗; 解京选; 刘彦强

    2011-01-01

    Coking with briquette coal blending process was an effective way to solve the shortage of China's high-quality and environmentally friendly coking coal.The production process and principles were well summarized,and a suitable process for the technological transformation of a coking company was proposed.Considering the life-span of coke oven and quality of coke,a reasonable rang(15%~30%) was found by experiments,as well as the positive effect of every kind of coal used to be coking.%配型煤炼焦是解决我国优质环保炼焦煤紧缺的有效途径。本文综述了配型煤炼焦技术的生产工艺及原理,给出了适合焦化厂技术改造的工艺流程。结合试验研究,考虑到焦炉的寿命和焦炭的质量,确定型煤配比的合理选择范围为15%~30%,并阐述了单种煤配型煤炼焦的效果。

  17. Clean Processing and Utilization of Coal Energy

    Institute of Scientific and Technical Information of China (English)

    陈如清; 王海峰

    2006-01-01

    The dominant status of coal on the energy production and consumption structure of China will not be changed in the middle period of this century. To realize highly efficient utilization of coal, low pollution and low cost are great and impendent tasks. These difficult problems can be almost resolved through establishing large-scale pithead power stations using two-stage highly efficient dry coal-cleaning system before coal burning, which is a highly efficient, clean and economical strategy considering the current energy and environmental status of China. All these will be discussed in detail in this paper.

  18. An experimental and numerical study of water jet cleaning process

    CERN Document Server

    Guha, Anirban; Balachandar, Ram

    2010-01-01

    In this paper, we have experimentally, numerically and theoretically investigated the water jet cleaning process. Very high speed water jets (~80-200 m/s) are used in such cleaning operations. These jets diffuse in the surrounding atmosphere by the process of air entrainment and this contributes to the spreading of the jet and subsequent decay of pressure. Estimation of this pressure decay and subsequent placement of the cleaning object is of paramount importance in manufacturing and material processing industries. Also, the pressure distribution on the cleaning surface needs to be assessed in order to understand and optimize the material removal process. Experimental study is performed to understand the pressure characteristics. A Semi-empirical model for capturing the air entrainment has been added to the commercial CFD package FLUENT. The simulation results are validated against ours as well as previous experimental findings. The numerical results have shown that the optimal stand-off distance in cleaning ...

  19. The effective carbonaceous restorer for the production of silicon carbide on the basis of deep processing of petroleum coke

    International Nuclear Information System (INIS)

    The skilled use of all particle size distribution of petroleum coke is considered. The different technologies of petroleum coke breeze ennoblement are shown and their advantages and weaknesses are identified. An optimal variant of preparation of petroleum coke breeze at the site attached to reactor for the production of silicon carbide is proposed. (authors)

  20. The mechanism of coking pressure generation II: Effect of high volatile matter coking coal, semi-anthracite and coke breeze on coking pressure and contraction

    Energy Technology Data Exchange (ETDEWEB)

    Merrick Mahoney; Seiji Nomura; Koichi Fukuda; Kenji Kato; Anthony Le Bas; David R. Jenkins; Sid McGuire [BHP Billiton Technology, Shortland, NSW (Australia)

    2010-07-15

    One of the most important aspects of the cokemaking process is to control and limit the coking pressure since excessive coking pressure can lead to operational problems and oven wall damage. Following on from a previous paper on plastic layer permeability we have studied the effect of contraction of semi-coke on coking pressure and the effect of organic additives on contraction. A link between contraction (or simulated contraction) outside the plastic layer and coking pressure was demonstrated. The interaction between this contraction, local bulk density around the plastic layer and the dependence of the permeability of the plastic layer on bulk density was discussed as possible mechanisms for the generation of coking pressure. The effect of blending either a high volatile matter coal or one of two semi-anthracites with low volatile matter, high coking pressure coals on the coking pressure of the binary blends has been explained using this mechanism. 25 refs., 10 figs., 4 tabs.

  1. Thermal and hydraulic effects of coke deposit in hydrocarbon pyrolysis process

    OpenAIRE

    Gascoin, Nicolas; Abraham, Grégory; Gillard, Philippe

    2012-01-01

    International audience Fuel pyrolysis can be of benefit for regenerative cooling techniques due to its endothermic effect in ensuring the thermal resistance of hypersonic vehicles and structures. Among pyrolysis species production, there is that of coke formation. A numerical code is used in this paper to investigate the related phenomena, based on two experiments using Titanium (Ti) and Stainless Steel (SS) reactors, which present different pyrolysis rates under similar operating conditio...

  2. Naphthenic acids speciation and removal during petroleum-coke adsorption and ozonation of oil sands process-affected water.

    Science.gov (United States)

    Gamal El-Din, Mohamed; Fu, Hongjing; Wang, Nan; Chelme-Ayala, Pamela; Pérez-Estrada, Leonidas; Drzewicz, Przemysław; Martin, Jonathan W; Zubot, Warren; Smith, Daniel W

    2011-11-01

    The Athabasca Oil Sands industry produces large volumes of oil sands process-affected water (OSPW) as a result of bitumen extraction and upgrading processes. Constituents of OSPW include chloride, naphthenic acids (NAs), aromatic hydrocarbons, and trace heavy metals, among other inorganic and organic compounds. To address the environmental issues associated with the recycling and/or safe return of OSPW into the environment, water treatment technologies are required. This study examined, for the first time, the impacts of pretreatment steps, including filtration and petroleum-coke adsorption, on ozonation requirements and performance. The effect of the initial OSPW pH on treatment performance, and the evolution of ozonation and its impact on OSPW toxicity and biodegradability were also examined. The degradation of more than 76% of total acid-extractable organics was achieved using a semi-batch ozonation system at a utilized ozone dose of 150 mg/L. With a utilized ozone dose of 100 mg/L, the treated OSPW became more biodegradable and showed no toxicity towards Vibrio fischeri. Changes in the NA profiles in terms of carbon number and number of rings were observed after ozonation. The filtration of the OSPW did not improve the ozonation performance. Petroleum-coke adsorption was found to be effective in reducing total acid-extractable organics by a 91%, NA content by an 84%, and OSPW toxicity from 4.3 to 1.1 toxicity units. The results of this study indicate that the combination of petroleum-coke adsorption and ozonation is a promising treatment approach to treat OSPW. PMID:21907388

  3. Easy to clean nanocomposite metal coatings for food processing

    OpenAIRE

    Becker-Willinger, Carsten; Heppe, Gisela; Krämer, Pamela; Schmidt, Helmut K.

    2002-01-01

    Cleaning and keeping clean of food processing equipment is of extremely high importance for hygienic reasons and, in many cases, also a cost factor for the whole process. Various low surface free energy coatings have been developed which show an antiadhesive behaviour to grease or food components, such as mustard, ketchup or fruit juices, even if baked at elevated temperatures on the coating surface. These coatings are composed of sol-gel derived hybrid materials, ceramic nanoparticles for me...

  4. Removal of polycyclic aromatic hydrocarbons and phenols from coking wastewater by simultaneously synthesized organobentonite in a one-step process

    Institute of Scientific and Technical Information of China (English)

    Zhenhua Wu; Lizhong Zhu

    2012-01-01

    The optimal condition for a one-step process removing organic compounds from coiking wastewater by simultaneously synthesized organobentonite as a pretreatment was investigated.Results showed that sorption of organic compounds by organobentonite was positively correlated to the cation surfactant exchange on the bentonite and the octanol-water partition coefficient (Kow) of the solutes.With 0.75 g/L bentonite and 180 mg/L (60% of bentonite cation exchange capacity) cetyltrimethylammonium bromide,the removal efficiencies of the 16 polycyclic aromatic hydrocarbon (PAHs) specified by the US Environmental Protection Agency in coking waste0water except naphthalene were more than 90%,and that of benzo(a)pyrene was 99.5%.At the same time,the removal efficiencies of CODCr,NH3-N,volatile phenols,colour and turbidity were 28.6%,13.2%,8.9%,55% and 84.3%,respectively,and the ratio of BOD5/CODcr increased from 0.31 to 0.41.These results indicated that the one-step process had high removal efficiency for toxic and refractory hydrophobic organic compounds,and could improve the biodegradability of the coking wastewater.Therefore it could be a promising technology for the pretreatment of toxic and refractory organic wastewater.

  5. Toxicity of coke wastewater treated with advanced oxidation by Fenton process supported by ultrasonic field

    OpenAIRE

    Kwarciak-Kozłowska Anna; Krzywicka Aleksandra

    2016-01-01

    The aim of the presented study was to determine the toxicity of wastewater from the production of coke. The wastewater was treated with advanced oxidation involving ultrasonic field with Fenton’s reagent (the amplitude was 61.5 μm and sonication time 8 min). Two doses of iron and four doses of hydrogen peroxide were used. The amount of hydrogen peroxide was proportional to the value of the chemical oxygen demand of raw wastewater, ranging from COD/H2O2 ratio of 1:2.5 to 1:20. Two tests were u...

  6. Single Hole Bottom of Coking Chamber Brick Replacement Process%单孔炭化室底砖更换的工艺过程

    Institute of Scientific and Technical Information of China (English)

    吴安庆

    2012-01-01

    Coke oven is composed of a variety of refractory bricks of complex structure of industrial furnace.Coke oven in the production process for many reasons,will make the coke oven refractory brick erosion or damage occurs,in order to ensure continuous production of the coke oven,furnace body of the repair is generally in the hot repair under.The paper briefly introduces the single hole bottom of coking chamber brick replacing the whole process,for reference.%焦炉是由各种耐火砖砌筑而成结构复杂的工业窑炉。焦炉在生产过程中由于很多原因,会使焦炉耐火砖出现剥蚀或损坏,为了保证焦炉的连续生产,炉体的各项维修一般都在热态修补下进行。文章简要介绍了单孔炭化室底砖整体更换的工艺过程,供同行参考。

  7. Innovative technologies on fuel assemblies cleaning for sodium fast reactors: First considerations on cleaning process

    International Nuclear Information System (INIS)

    Within the framework of Sodium Fast Reactor development, innovative fuel assembly cleaning operations are investigated to meet the GEN IV goals of safety and of process development. One of the challenges is to mitigate the Sodium Water Reaction currently used in these processes. The potential applications of aqueous solutions of mineral salts (including the possibility of using redox chemical reactions) to mitigate the Sodium Water Reaction are considered in a first part and a new experimental bench, dedicated to this study, is described. Anhydrous alternative options based on Na/CO2 interaction are also presented. Then, in a second part, a functional study conducted on the cleaning pit is proposed. Based on experimental feedback, some calculations are carried out to estimate the sodium inventory on the fuel elements, and physical methods like hot inert gas sweeping to reduce this inventory are also presented. Finally, the implementation of these innovative solutions in cleaning pits is studied in regard to the expected performances. (authors)

  8. The cleaning process of metal surfaces in barrier discharge plasmas

    International Nuclear Information System (INIS)

    The cleaning process of metal surfaces was studied, which were used as one of the electrodes of planar barrier discharges. The barrier electrodes were made from ferroelectric ceramics. The discharges operated in flowing oxygen and air at atmospheric pressure. The metal probes were covered by defined layers of special oils. The dependence of the cleaning process on the gas flow was observed with optical emission spectroscopy. A clean surface has been reached only at low gas flows (1-5 l/h). At higher gas flows the lubricant could not be removed completely because of polymerization of the oil. With GC/MS capillary chromatography CO2 was detected as the final reaction product. The comparison of the cleaning effect in air and pure oxygen showed a higher efficiency of the air discharge. The surface situation was controlled by spectroscopic ellipsometry and XPS. (author)

  9. Performance evaluation of a full-scale coke oven wastewater treatment plant in an integrated steel plant.

    Science.gov (United States)

    Kumar, M Suresh; Vaidya, A N; Shivaraman, N; Bal, A S

    2003-01-01

    Wastewater generated during coke-oven gas cleaning operations in the integrated steel plant contains phenol, cyanide, thiocyanate, and also oil and grease. Although the activated sludge process is widely practiced for biological treatment of coke-oven wastewater, it was observed during the evaluation of performance of full scale coke-oven wastewater treatment plant that oil contamination and poor sludge settleability had resulted in poor maintenance of the activated sludge process. Keeping these aspects in view, treatability studies were conducted and an alternative treatment process is proposed. With these corrective measures the coke-oven wastewater treatment plant will give desired performance. In this paper we present results of the performance evaluation, data on treatability studies and alternative treatment process scheme. PMID:14723281

  10. Optoacoustic analysis of the laser-cleaning process

    OpenAIRE

    Bregar, Vladimir Boštjan; Možina, Janez

    2015-01-01

    Laser cleaning is an optodynamic process in which the optically induced removal of a liquid or a solid contaminant from a substrate is accompanied by a optoacoustic wave in the surrounding air. In our experiments we used both dry and steam laser-cleaning techniques for various samples. Optoacoustic wave, produced by the abrupt heating and detachment of the contaminants, was observed with a probe-beam deflection technique. We determined two characteristic parameters of the optoacoustic wave: t...

  11. Modeling the kinetics of methane conversion in steam reforming process of coke-oven gas based on experimental data

    Institute of Scientific and Technical Information of China (English)

    ZHANG Jia-yuan; ZHOU Jie-min

    2007-01-01

    Steam-reforming is an effective approach for upgrading methane and hydrocarbon of coke-oven gas into CO and H2, but the kinetic behavior needs more study. We investigated the conversion of methane in coke-oven gas by steam reforming process in an electric tubular flow at 14 kPa with temperature varying from 500℃ to 950℃, and developed a kenetic model for , ignoring the effects of adsorption and diffusion. The optimal dynamic conditions for methane conversion 14 kPa are as follows: the ratio of the amount of water to the amount of methane is from 1.1 to 1.3; the reaction temperature is from 1 223 K to 1 273 K. The methane conversion rate is larger than 95% when the ratio of the amount of water to the amount of methane is 1.2 at a temperature above 1 223 K with the residence time up to 0.75 s.

  12. Substitution of Organic Solvents in Selected Industrial Cleaning Processes

    DEFF Research Database (Denmark)

    Jacobsen, Thomas; Rasmussen, Pia Brunn

    1997-01-01

    can be replaced with monoesters of fatty acids from vegetable oils (VOFA). The paper describes the selection of other industrial cleaning or degreasing processes where VOC could be replaced by VOFA. Manual degreasing and cleaning processes in metal industry, maintenance and repair of vehicles, and...... industrial coating processes are likely candidates for substitution of VOC with VOFA. Requirements to the resulting surfaces may, however, hinder the replacement. This is especially important when the surface has to be coated in a subsequent step.......Volatile organic solvents (VOC)are becoming increasingly unwanted in industrial processes. Substitution of VOC with non-volatile, low-toxic compounds is a possibility to reduce VOC-use. It has been successfully demonstrated, that organic solvents used in cleaning processes in sheet offset printing...

  13. Analysis of chemical coal cleaning processes. Final report

    Energy Technology Data Exchange (ETDEWEB)

    1980-06-01

    Six chemical coal cleaning processes were examined. Conceptual designs and costs were prepared for these processes and coal preparation facilities, including physical cleaning and size reduction. Transportation of fine coal in agglomerated and unagglomerated forms was also discussed. Chemical cleaning processes were: Pittsburgh Energy Technology Center, Ledgemont, Ames Laboratory, Jet Propulsion Laboratory (two versions), and Guth Process (KVB). Three of the chemical cleaning processes are similar in concept: PETC, Ledgemont, and Ames. Each of these is based on the reaction of sulfur with pressurized oxygen, with the controlling factor being the partial pressure of oxygen in the reactor. All of the processes appear technically feasible. Economic feasibility is less certain. The recovery of process chemicals is vital to the JPL and Guth processes. All of the processes consume significant amounts of energy in the form of electric power and coal. Energy recovery and increased efficiency are potential areas for study in future more detailed designs. The Guth process (formally designed KVB) appears to be the simplest of the systems evaluated. All of the processes require future engineering to better determine methods for scaling laboratory designs/results to commercial-scale operations. A major area for future engineering is to resolve problems related to handling, feeding, and flow control of the fine and often hot coal.

  14. Impact of a semi-industrial coke processing plant in the surrounding surface soil. Part II: PAH content

    OpenAIRE

    García Fernández, Roberto; Díaz Somoano, Mercedes; Calvo Díez, Montserrat; López Antón, María Antonia; Suárez, Sonia; Suárez Ruiz, Isabel; Martínez Tarazona, María Rosa

    2012-01-01

    Topsoil samples taken from different areas of a disused experimental coking plant were analysed in order to determine their polycyclic aromatic hydrocarbon (PAH) concentration. The variation in concentrations as a function of distance from the coking oven battery was studied and a reduction in PAH concentration as the distance to the coking ovens' battery increases was observed. Two exceptions are the area in the vicinity of the tar distillation section of the plant, with a strong contributio...

  15. Influence of low-density polyethylene addition on coking pressure

    OpenAIRE

    Melendi, Sonia; Barriocanal, C.; R. Alvarez; M.A. Diez

    2014-01-01

    Different amounts of low-density polyethylene (LDPE) were added to a bituminous coal used to produce metallurgical coke. The effect of the plastic waste on the carbonization process and more exactly, on the coking pressure were investigated. A movable wall oven at semi-pilot scale was used for measuring coking pressure generated. It was found that coking pressure increases for low LDPE addition levels (1-3 wt.%); however higher amounts of LDPE reduce coking pressure. To explain this behavior ...

  16. Fissure formation in coke. 2: Effect of heating rate, shrinkage and coke strength

    Energy Technology Data Exchange (ETDEWEB)

    D.R. Jenkins; M.R. Mahoney [CSIRO, North Ryde, NSW (Australia). Mathematical and Information Sciences

    2010-07-15

    We investigate the effects of the heating rate, coke shrinkage and coke breakage strength upon the fissure pattern developed in a coke oven charge during carbonisation. This is done principally using a mechanistic model of the formation of fissures, which considers them to be an array of equally spaced fissures, whose depth follows a 'period doubling' pattern based upon the time history of the fissures. The model results are compared with pilot scale coke oven experiments. The results show that the effect of heating rate on the fissure pattern is different to the effect of coke shrinkage, while the effect of coke breakage strength on the pattern is less pronounced. The results can be seen in both the shape and size of resulting coke lumps after stabilisation. The approach gives the opportunity to consider means of controlling the carbonisation process in order to tune the size of the coke lumps produced. 7 refs., 18 figs., 4 tabs.

  17. APPLICABILITY OF COKE PLANT CONTROL TECHNOLOGIES TO COAL CONVERSION

    Science.gov (United States)

    The report gives results of comparisons of process and waste stream characteristics from the Byproduct coke over process with selected gasification and liquefaction processes. It includes recommendations regarding control technologies for air, water, and solid wastes. Coke oven c...

  18. 对各种炼焦工艺及无回收焦炉的评述%Commentary on Various Cokemaking Process and No Recovery Coke Oven Batteries

    Institute of Scientific and Technical Information of China (English)

    钟英飞

    2001-01-01

    The present developing situation and direction of cokemaking processes in the counties all over the world is described and comment is made mainly on the advantages and disadvantages of no recovery coke oven batteries and on the limitation of no recovery coke oven battery developing in our country.%介绍了世界各国炼焦工艺的开发现状及发展方向,重点评述了无回收焦炉的优缺点,及在我国发展无回收焦炉的局限性。

  19. Toxicity of coke wastewater treated with advanced oxidation by Fenton process supported by ultrasonic field

    Directory of Open Access Journals (Sweden)

    Kwarciak-Kozłowska Anna

    2016-03-01

    Full Text Available The aim of the presented study was to determine the toxicity of wastewater from the production of coke. The wastewater was treated with advanced oxidation involving ultrasonic field with Fenton’s reagent (the amplitude was 61.5 μm and sonication time 8 min. Two doses of iron and four doses of hydrogen peroxide were used. The amount of hydrogen peroxide was proportional to the value of the chemical oxygen demand of raw wastewater, ranging from COD/H2O2 ratio of 1:2.5 to 1:20. Two tests were used to determine the toxicity (algae growth inhibition test and Lepidium test. It was found that more toxic to algae was wastewater treated by Fenton’s reagent containing a higher dose of iron. A similar inhibitory effect was observed on the germination of cress seeds.

  20. Treatment of coke-oven wastewater with the powdered activated carbon-contact stabilization activated sludge process. Final report

    Energy Technology Data Exchange (ETDEWEB)

    Suidan, M.T.; Deady, M.A.; Gee, C.S.

    1983-11-01

    The objective of the study was to determine optimum parameters for the operation of an innovative process train used in the treatment of coke-over wastewater. The treatment process train consisted of a contact-stabilization activated sludge system with powdered activated carbon (PAC) addition, followed by activated sludge nitrification, followed by denitrification in an anoxic filter. The control and operating parameters evaluated during the study were: (a) the average mixed-liquor PAC concentration maintained in the contact-stabilization system, (b) the solids retention time practiced in the contact-stabilization system, and (c) the hydraulic detention time maintained in the contact aeration tank. Three identical treatement process trains were constructed and employed in this study. The coke-oven wastewater used for this investigation was fed to the treatment units at 30% strength. The first part of the study was devoted to determining the interactions between the mixed liquor PAC concentration and the solids retention time in the contact-stabilization tanks. Results showed that optimum overall system performance is attainable when the highest sludge age (30 day) and highest mixed liquor PAC concentration were practiced. During the second phase of the study, all three systems were operated at a 30 day solids retention time while different detention times of 1, 2/3 and 1/3 day were evaluated in the contact tank. PAC addition rates were maintained at the former levels and, consequently, reduced contact times entailed higher mixed liquor carbon concentrations. Once again, the system receiving the highest PAC addition rate of PAC exhibited the best overall performance. This system exhibited no deterioration in process performance as a result of decreased contact detention time. 72 references, 41 figures, 24 tables.

  1. Alternative, Green Processes for the Precision Cleaning of Aerospace Hardware

    Science.gov (United States)

    Maloney, Phillip R.; Grandelli, Heather Eilenfield; Devor, Robert; Hintze, Paul E.; Loftin, Kathleen B.; Tomlin, Douglas J.

    2014-01-01

    Precision cleaning is necessary to ensure the proper functioning of aerospace hardware, particularly those systems that come in contact with liquid oxygen or hypergolic fuels. Components that have not been cleaned to the appropriate levels may experience problems ranging from impaired performance to catastrophic failure. Traditionally, this has been achieved using various halogenated solvents. However, as information on the toxicological and/or environmental impacts of each came to light, they were subsequently regulated out of use. The solvent currently used in Kennedy Space Center (KSC) precision cleaning operations is Vertrel MCA. Environmental sampling at KSC indicates that continued use of this or similar solvents may lead to high remediation costs that must be borne by the Program for years to come. In response to this problem, the Green Solvents Project seeks to develop state-of-the-art, green technologies designed to meet KSCs precision cleaning needs.Initially, 23 solvents were identified as potential replacements for the current Vertrel MCA-based process. Highly halogenated solvents were deliberately omitted since historical precedents indicate that as the long-term consequences of these solvents become known, they will eventually be regulated out of practical use, often with significant financial burdens for the user. Three solvent-less cleaning processes (plasma, supercritical carbon dioxide, and carbon dioxide snow) were also chosen since they produce essentially no waste stream. Next, experimental and analytical procedures were developed to compare the relative effectiveness of these solvents and technologies to the current KSC standard of Vertrel MCA. Individually numbered Swagelok fittings were used to represent the hardware in the cleaning process. First, the fittings were cleaned using Vertrel MCA in order to determine their true cleaned mass. Next, the fittings were dipped into stock solutions of five commonly encountered contaminants and were

  2. RESEARCH ON THE QUALITY PRICE RATIO OF COKING COAL

    Institute of Scientific and Technical Information of China (English)

    陶树人; 王永君

    1994-01-01

    If assortment price parity of Clean coling coal and its quallty price difference is nonreasortable, it doesn't guide in improving the qualiry metaljurgical eoking coal and may be influence the economic benefit of metallurgical enterprises. This paper propose the principles and mathematic model for determination assortment parity of ciean cokingcoal and its quality difference of ash content in clean coking coa in order to urge wasberies into producing superior clean coking coal which is under condition of consideration both intorest waskcries and interest metallurgical industry. It canbe used as a method in theory to make price stra,iegics under condition of socialism maket economic for washeries of clean coking coal

  3. Physico-chemical characterization of products from vacuum oil under delayed coking process by infrared spectroscopy and chemometrics methods

    Science.gov (United States)

    Meléndez, L. V.; Cabanzo, R.; Mejía-Ospino, E.; Guzmán, A.

    2016-02-01

    Eight vacuum residues and their delayed coking liquids products from Colombian crude were study by infrared spectroscopy with attenuated total reflectance (FTIR-ATR) and principal component analysis (PCA). For the samples the structural parameters of aromaticity factor (fa), alifaticity (A2500-3100cm-1), aromatic condensation degree (GCA), length of aliphatic chains (LCA) and aliphatic chain length associated with aromatic (LACAR) were determined through the development of a methodology, which includes the previous processing of spectroscopy data, identifying the regions in the IR spectra of greatest variance using PCA and molecules patterns. The parameters were compared with the results obtained from proton magnetic resonance (1H-NMR) and 13C-NMR. The results showed the influence and correlation of structural parameters with some physicochemical properties such as API gravity, weight percent sulphur (% S) and Conradson carbon content (% CCR)

  4. K2CO3 catalysis on the reactivity of top charged coke and stamp charged coke

    Science.gov (United States)

    Pang, Qing-hai; Zhang, Jian-liang; Qi, Cheng-lin; Ma, Chao; Kong, De-wen; Mao, Rui

    2013-01-01

    The catalysis of K2CO3 on the reactivity of top charged coke and stamp charged coke from Pansteel in China was studied. The coke reaction index of the stamp charged coke was 1%-2% higher than that of the top charged coke. Under the catalysis of K2CO3, the coke reaction index of both cokes approximately increased by 4%, 6%, 10% and 6% at 900, 1000, 1100 and 1200°C, respectively. The reactivity of the K-enriched stamp charged coke was 1%-2% higher than that of the K-enriched top charged coke below 1100°C. However, only negligible differences were found in the temperature zone between 1100 and 1200°C. Scanning electron microscopy images illustrated that pores in the top charged coke were smaller and equally distributed, while relatively more big pores exist non-homogenously in stamp charged coke. Due to the different processes in production, the stamp charged coke was more porous and most of the pores tended to be applanate. Cracks were observed in the microstructure of the stamp charged coke during the carbon solution reaction, implying the inferior quality of the stamp charged coke to the top charged coke at high temperature. Diffusion of K during the carbon solution reaction was studied by the energy dispersive spectrometry. It is found that K gradually spreads into the center of lumpy coke with the rising of temperature and is equally distributed on the edges of pores at 1200°C. Besides, oxidation reactions of functional groups become faster with the catalysis of K.content

  5. NATO/CCMS PILOT STUDY - CLEAN PRODUCTS AND PROCESSES

    Science.gov (United States)

    The proposed objective of the NATO/CCMS Pilot on clean products and processes is to facilitate further gains in pollution prevention, waste minimization, and design for the environment. It is anticipated that the free exchange of knowledge, experience, data, and models will fost...

  6. Flue Gas Cleaning With Alternative Processes and Reaction Media

    DEFF Research Database (Denmark)

    Rasmussen, Søren Birk; Huang, Jun; Riisager, Anders; Hamma-Cugny, Hind; Rogez, Jacquez; Winnick, J.; Wassserscheid, Peter; Fehrmann, Rasmus

    2007-01-01

    Alternative methods to the traditional industrial NOX and SOXflue gas cleaning processes working at lower temperatures and/orleading to useful products are desired. In this work we presentour latest results regarding the use of molten ionic media inelectrocatalytic membrane separation, ionic liquid...

  7. Effect of the catalyzing combustion of coke breeze on the energy saving in sinter process

    Institute of Scientific and Technical Information of China (English)

    2001-01-01

    The mechanism of additive ZC-1 for catalyzing combustion of coke breeze in sintering of iron one fines was studied by using X-ray Diffraction, TGA and GC (Gas Chromatographer), by which energy saving was achieved on sinter pot test. The results show that the distance between cleavage planes is enlarged and the π-electrons are re-distibuted because of the insertion of cations/molecules of ZC-1 into the cleavage planes of carbon , resulting in the weakening of C-C bond, improving the adsorption of oxygen and lowering the activation energy of gasification of carbon from 25.8 kJ/mol to 18.9 kJ/mol , and the burning rate being increased and combustion residual reduced, all of which can lead to lower solid fuel consumption . Compared with the sintering test without addition of additives , the solid fuel consumption is reduced by 16.0%, meanwhile, the rate of finished sinter, the output of finished sinter and the tumbling index are increased by 2.03%, 7.0% and 3.71%, respectively, with incorporating 0.2% of additive ZC-1 in the sintering mixture, which is in agreement with the catalyzing mechanism of ZC-1.

  8. Determination of a cleaning and decontamination process using solvents

    International Nuclear Information System (INIS)

    This work has been carried out on samples of the white cotton serge material of which most of the working overalls of the Nuclear Research Centre are made. The aims are: - to determine,from the decontamination and cleaning points of view, the efficiency of various solvents (white-spirit, trichloroethylene, perchlorethylene and tri-chloro-trifluoroethane) and the role of additives likely to improve the treatment; - to control the textile from the wear and shrinkage points of view; - to try to develop a basic cleaning and decontamination process as a function of the possibilities of each solvent considered. (authors)

  9. Characterization of the cleaning process on a transferred graphene

    International Nuclear Information System (INIS)

    Intrinsic graphene possesses many outstanding physical and chemical properties, but their full explorations are often hindered by the effects of substrate and/or contamination. The authors employ the ultrahigh vacuum transmission electron microscopy equipped with a residual gas analyzer to in-situ characterize an effective decontamination process on a suspended graphene. Raman spectroscopic spectra further verify the cleanness of the resultant graphene membrane. The authors also present two contrasting growth morphologies of copper nanoparticles obtained on both clean and unclean graphene surfaces and show that the intrinsic growth dynamics can only manifest on the surface without contaminations

  10. Alternatives to Organic Solvents in Industrial Cleaning Processes

    DEFF Research Database (Denmark)

    Jacobsen, Thomas

    1998-01-01

    cleaning agents in offset printing companies instead of volatile, toxic organic solvents. The present study is based on a project with the aim of defining other industrial processes, where organic solvents used for cleaning or degreasing can be replaced by non-volatile, low-toxic products, which are based...... on esters from fatty acids of vegetable origin (vegetable esters - VE).The study indicates that industrial cleaning/degreasing with organic solvents may be substituted with VEs on metal surfaces and on some coated surfaces, in manufacture of paints and inks, use of paints, use of inks (printing......), metal industry, and vehicle repair and maintenance. There are, however, other elements that influence the possibility to substitute. The requirements to the resulting surface, depending on the following treatment of the surface. The character of the soilings to be removed. The possible presence of other...

  11. Coke dust enhances coke plant wastewater treatment.

    Science.gov (United States)

    Burmistrz, Piotr; Rozwadowski, Andrzej; Burmistrz, Michał; Karcz, Aleksander

    2014-12-01

    Coke plant wastewater contain many toxic pollutants. Despite physico-chemical and biological treatment this specific type of wastewater has a significant impact on environment and human health. This article presents results of research on industrial adsorptive coke plant wastewater treatment. As a sorbent the coke dust, dozen times less expensive than pulverized activated carbon, was used. Treatment was conducted in three scenarios: adsorptive after full treatment with coke dust at 15 g L(-1), biological treatment enhanced with coke dust at 0.3-0.5 g L(-1) and addition of coke dust at 0.3 g L(-1) prior to the biological treatment. The enhanced biological treatment proved the most effective. It allowed additional removal of 147-178 mg COD kg(-1) of coke dust. PMID:25113994

  12. Design Fuels Corporation (DFC)-Apache, Inc. coal reclamation system for the plant of the future for processing clean coal

    International Nuclear Information System (INIS)

    The mechanical washing processing and drying portion of the DFC process offers an efficient method for cleaning of pyritic sulfur bearing compounds which represents 25% sulfur reduction from original run-of-mine coal quality. This reduction can be augmented with the use of calcium and sodium based compounds to reduce the sulfur in many coals to produce compliance quality coal. The use of mechanical/physical methods for the removal of the pyritic material found in coal is used by the DFC process as a first step to the final application of a complete coal refuse clean-up technology based on site specific conditions of the parent coal. The paper discusses the use of the DFC process to remediate slurry ponds and tailings piles and to improve coal cleaning by gravity separation methods, flotation, hydrocyclones and spiral separators, dense media separation, water only cyclones, and oil/solvent agglomeration. A typical DFC Project is the Rosa Coal Reclamation Project which involves the development of a bituminous coal waste impoundment reclamation and washery system. The plant would be located adjacent to a coal fines pond or tailings pond and refuse pile or gob pile at a former coal strip mine in Oneonta, Alabama. Design Fuels would provide a development program by which coal waste at the Rosa Mine could be reclaimed, cleaned and sold profitably. This feedstock could be furnished from recovered coal for direct use in blast furnaces, or as feedstock for coke ovens at 250,000 tons per year at an attractive price on a 10-year contract basis. The site has an old coal washing facility on the property that will be dismantled. Some equipment salvage has been considered; and removal of the existing plant would be the responsibility of Design Fuels. The paper briefly discusses the market potential of the process

  13. Northwestern University Facility for Clean Catalytic Process Research

    Energy Technology Data Exchange (ETDEWEB)

    Marks, Tobin Jay [Northwestern University

    2013-05-08

    Northwestern University with DOE support created a Facility for Clean Catalytic Process Research. This facility is designed to further strengthen our already strong catalysis research capabilities and thus to address these National challenges. Thus, state-of-the art instrumentation and experimentation facility was commissioned to add far greater breadth, depth, and throughput to our ability to invent, test, and understand catalysts and catalytic processes, hence to improve them via knowledge-based design and evaluation approaches.

  14. Conceptual design of coke-oven gas assisted coal to olefins process for high energy efficiency and low CO2 emission

    International Nuclear Information System (INIS)

    Highlights: • A novel coke-oven gas assisted coal to olefins (GaCTO) process is proposed. • GaCTO has higher energy efficiency and emits less CO2 compared to coal-to-olefins process. • GaCTO proposes an idea of using redundant coke-oven gas for producing value added products. - Abstract: Olefins are one of the most important platform chemicals. Developing coal-to-olefins (CTO) processes is regarded as one of promising alternatives to oil-to-olefins process. However, CTO suffers from high CO2 emission due to the high carbon contents of coal. In China, there is 7 × 1010 m3 coke-oven gas (COG) produced in coke plants annually. However, most of the hydrogen-rich COG is utilized as fuel or discharged directly into the air. Such situation is a waste of precious hydrogen resource and serious economic loss, which causes serious environmental pollution either. This paper proposes a novel co-feed process of COG assist CTO in which CH4 of COG reacts with CO2 in a Dry Methane Reforming unit to reduce emissions, while the Steam Methane Reforming unit produces H2-rich syngas. H2 of COG can adjust the H/C ratio of syngas. The analysis shows that the energy efficiency of the co-feed process increases about 10%, while at the same time, life cycle carbon footprint is reduced by around 85% in comparison to the conventional CTO process. The economic sustainability of the co-feed process will be reached when the carbon tax would be higher than 150 CNY/t CO2

  15. Development of reduced crude processing technology in delayed coking units; Desenvolvimento da tecnologia de processamento de residuo atmosferico em unidade de coqueamento retardado

    Energy Technology Data Exchange (ETDEWEB)

    Soares, Gloria Maria Gomes; Bartros, Francisco Carlos da Costa; Goncalves, Natalie Jorge; Pala, Danielle Marins; Nadolni, Aline Voigt [PETROBRAS, Rio de Janeiro, RJ (Brazil)

    2008-07-01

    Delayed Coking Technology can be described as thermal cracking of low value refinery residual streams into high-value products. This process has been applied in petroleum refining schemes in order to upgrade heavy and ultra-heavy crude oils. The typical feedstock is vacuum residue (VR). When we have an increasing medium distillates demand and refining schemes which have gas oil and VR excess, the simultaneous conversion of these streams becomes economically attractive, due mainly to the increase of diesel production. Thus, the processing of atmospheric residue (AR) in Delayed Coking Units (DCU) has fueled great interest for PETROBRAS. This work presents the results of industrial and pilot plant tests with AR and VR showing the increasing of diesel yields and decreasing of coke yields processing AR as feedstock. When we process all the AR in the DCU with high recycle rate we observe an increasing of 25% on refinery diesel production related to conventional schemes. The refining scheme of the new PETROBRAS refinery at Northeast of Brazil is based on this technology. This refinery will process heavy oils maximizing diesel production with minimum investment. (author)

  16. Study of the aerobic biodegradation of coke wastewater in a two and three-step activated sludge process

    International Nuclear Information System (INIS)

    A laboratory-scale biological plant composed of two aerobic reactors operating at 35 deg. C was used to study the biodegradation of coke wastewater. The main pollutants to be removed are organic matter, especially phenols, thiocyanate and ammonium nitrogen. The concentrations of the main pollutants in the wastewater during the study ranged between 922 and 1980 mg COD/L, 133 and 293 mg phenol/L, 176 and 362 mg SCN/L and 123 and 296 mg NH4+-N/L. The biodegradation of these pollutants was studied employing different hydraulic residence times (HRT) and final effluent recycling ratios in order to minimize inhibition phenomena attributable to the high concentrations of pollutants. During the optimisation of the operating conditions, the removal of COD, phenols and thiocyanate was carried out in the first reactor and the nitrification of ammonium took place in the second. The best results were obtained when operating at an HRT of 98 h in the first reactor and 86 h in the second reactor, employing a recycling ratio of 2. The maximum removal efficiencies obtained were 90.7, 98.9, 98.6 and 99.9% for COD, phenols, thiocyanate and NH4+-N, respectively. In order to remove nitrate, an additional reactor was also implemented to carry out the denitrification process, adding methanol as an external carbon source. Very high removal efficiencies (up to 99.2%) were achieved

  17. MEDIUM PRESSURE HYDROUPGRADING PROCESS (MHUG) AND PRODUCTION OF CLEAN FUELS

    Institute of Scientific and Technical Information of China (English)

    2001-01-01

    The medium pressure hydroupgrading process (MHUG) unit with an 800 kt/a processing capacity of Jinzhou Petrochemical Company is used to hydroupgrade the mixture of FCC LCO fuel and straight-run diesel fuel in the presence of RN/RT series catalysts for improvement of the quality of the diesel fuel. Meanwhile, catalytic reforming feedstock is also obtained. The sulfur, nitrogen and aromatics contained in the hydroupgraded diesel fuel products can be minimized and the cetane number can be heightened. The produced clean fuels can meet the requirements of environmental protection.

  18. Properties of Spent Active Coke Particles Analysed via Comminution in Spouted Bed

    Science.gov (United States)

    Buczek, Bronislaw

    2013-01-01

    Samples of active coke, fresh and spent after cleaning flue gases from communal waste incinerators, were investigated. The outer layers of both coke particles were separately removed by comminution in a spouted bed. The samples of both active cokes were analysed by means of densities, mercury porosimetry, and adsorption technique. Remaining cores were examined to determine the degree of consumption of coke by the sorption of hazardous emissions (SO2, HCl, and heavy metals) through its bed. Differences in contamination levels within the porous structure of the particles were estimated. The study demonstrated the effectiveness of commercial active coke in the cleaning of flue gases. PMID:24459454

  19. Properties of spent active coke particles analysed via comminution in spouted bed.

    Science.gov (United States)

    Buczek, Bronislaw

    2013-01-01

    Samples of active coke, fresh and spent after cleaning flue gases from communal waste incinerators, were investigated. The outer layers of both coke particles were separately removed by comminution in a spouted bed. The samples of both active cokes were analysed by means of densities, mercury porosimetry, and adsorption technique. Remaining cores were examined to determine the degree of consumption of coke by the sorption of hazardous emissions (SO2, HCl, and heavy metals) through its bed. Differences in contamination levels within the porous structure of the particles were estimated. The study demonstrated the effectiveness of commercial active coke in the cleaning of flue gases. PMID:24459454

  20. Physico-chemical treatment of coke plant effluents for control of water pollution in India

    Energy Technology Data Exchange (ETDEWEB)

    Ghose, M.K. [Indian School of Mines, Dhanbad (India). Center of Mining Environmental

    2002-01-01

    Coal carbonizing industries in India are important and are growing every year. Large quantities of liquid effluents produced in this industry contain a large amount of suspended solids, high biochemical oxygen demand (BOD), chemical oxygen demand (COD), phenols, ammonia and other toxic substances, which are causing serious surface water pollution in the area. There is a large number of coke plants in the vicinity of Jharia Coal Field (JCF). The working principle of a coke plant and the effluents produced is described. One large coke plant was chosen to evaluate characteristics of the effluent and to suggest a proper treatment method. Present effluent treatment system was found to be inadequate and a large quantity of a very good quality coke breeze is being lost, which is also causing siltation on the riverbed in addition to surface water pollution. Physico-chemical treatment has been considered as a suitable option for the treatment of coke plant effluents. A scheme has been proposed for the treatment, which can be suitably adopted for the recycling, reuse or safe disposal of the treated effluent. Various unit process and unit operations are discussed. The process may be useful on industrial scale for various sites so as to maintain a clean environment.

  1. Self Cleaning HEPA Filtration without Interrupting Process Flow

    International Nuclear Information System (INIS)

    The strategy of protecting the traditional glass fibre HEPA filtration train from it's blinding contamination and the recovery of dust by the means of self cleaning, pre-filtration is a proven means in the reduction of ultimate disposal volumes and has been used within the Fuel Production Industry. However, there is an increasing demand in nuclear applications requiring elevated operating temperatures, fire resistance, moisture resistance and chemical composition that the existing glass fibre HEPA filtration cannot accommodate, which can be remedied by the use of a metallic HEPA filter media. Previous research (Bergman et al 1997, Moore et al 1992) suggests that the then costs to the DOE, based on a five year life cycle, was $29.5 million for the installation, testing, removal and disposal of glass fibre HEPA filtration trains. Within these costs, $300 was the value given to the filter and $4,450 was given to the peripheral activity. Development of a low cost, cleanable, metallic, direct replacement of the traditional filter train will the clear solution. The Bergman et al work has suggested that a 1000 ft3/min, cleanable, stainless HEPA could be commercially available for $5,000 each, whereas the industry has determined that the truer cost of such an item in isolation would be closer to $15,000. This results in a conflict within the requirement between 'low cost' and 'stainless HEPA'. By proposing a system that combines metallic HEPA filtration with the ability to self clean without interrupting the process flow, the need for a tradition HEPA filtration train will be eliminated and this dramatically reduces the resources required for cleaning or disposal, thus presenting a route to reducing ultimate costs. The paper will examine the performance characteristics, filtration efficiency, flow verses differential pressure and cleanability of a self cleaning HEPA grade sintered metal filter element, together with data to prove the contention. (authors)

  2. Properties of Spent Active Coke Particles Analysed via Comminution in Spouted Bed

    OpenAIRE

    Bronislaw Buczek

    2013-01-01

    Samples of active coke, fresh and spent after cleaning flue gases from communal waste incinerators, were investigated. The outer layers of both coke particles were separately removed by comminution in a spouted bed. The samples of both active cokes were analysed by means of densities, mercury porosimetry, and adsorption technique. Remaining cores were examined to determine the degree of consumption of coke by the sorption of hazardous emissions (SO2, HCl, and heavy metals) through its bed. Di...

  3. Discussion about Saving Energy Technology in Coke Oven Gas Purification Process%焦炉煤气净化工艺节能技术探讨

    Institute of Scientific and Technical Information of China (English)

    李训明; 郭凤明; 董佃滨; 张长征

    2014-01-01

    Some technology applications in coke oven gas purification process were described , such as full negative pressure gas purification , negative pressure distillation , heat pump , etc.The role of these technologies was analyzed in terms of energy -saving emission reduction and efficient production , etc.There was high resource consumption , outstanding environmental protection problems in coking industry.Reasonably arranging , efficiently utilizing the energy generated in the process to reduce energy waste contributed to the harmonious development of resources and products and environment in coking enterprises.%介绍了焦炉煤气净化工艺中全(半)负压煤气净化、负压蒸馏、热泵等技术的应用,分析了这些技术在节能减排、高效生产等方面的作用。对资源消耗高,环保问题突出的焦化行业而言,工艺过程中产生的能量加以合理安排,高效利用,减少能源浪费,有助于焦化企业资源-产品-环境和谐发展。

  4. A chemical cleaning process with Cerium (IV)-sulfuric acid

    International Nuclear Information System (INIS)

    A chemical cleaning process with a high decontamination factor (DF) is requested for decommissioning. Usually, the process should be qualified with the features, such as the feasibility of treating large or complicated form waste, the minimization of secondary waste. Therefore, a powerful technique of redox decontamination process with Ce+4/Ce+3 has been studied at INER. First, the redox of cerium ion with electrolytic method was developed. Two kinds of home-made electrolyzer were used. One is with an ion-exchange membrane, and the other one is with a ceramic separator. Second, factors influencing the decontamination efficiency, such as the concentration of Ce+4, regeneration current density, temperature, acidity of solution were all studied experimentally, and the optimum conditions were specified too. Third, the liquid waste recycling and treatment were developed with electrodialysis and ion-exchange absorption methods. Finally, the hot test was proceeded with the contaminated metals from DCR of nuclear facility. (author)

  5. Naphthalene derivatives in the MTO process from a molecular modeling perspective: reactive species or coke?

    OpenAIRE

    Nollet, Arno; Hemelsoet, Karen; Lesthaeghe, David; Van Speybroeck, Veronique; WAROQUIER, MICHEL

    2009-01-01

    Currently, basic chemicals in polymer industry are mainly produced by thermal cracking of petroleum, but a promising alternative has been found: methanol-to-olefins (MTO). Methanol can be made from natural gas via syngas, but also from biomass. Molecular modeling of the MTO process has been a challenging topic, yet the reaction mechanism of the active route is starting to get unraveled based on the ‘hydrocarbon pool’ hypothesis [1], where aromatic species play a fundamental role as co-catalyt...

  6. A Hybrid Gas Cleaning Process for Production of Ultraclean Syngas

    Energy Technology Data Exchange (ETDEWEB)

    Merkel, T.C.; Turk, B.S.; Gupta, R.P.; Cicero, D.C.; Jain, S.C.

    2002-09-20

    The overall objective of this project is to develop technologies for cleaning/conditioning IGCC generated syngas to meet contaminant tolerance limits for fuel cell and chemical production applications. The specific goals are to develop processes for (1) removal of reduced sulfur species to sub-ppm levels using a hybrid process consisting of a polymer membrane and a regenerable ZnO-coated monolith or a mixed metal oxide sorbent; (2) removal of hydrogen chloride vapors to sub-ppm levels using an inexpensive, high-surface-area material; and (3) removal of NH3 with acidic adsorbents followed by conversion of this NH3 into nitrogen and water. Existing gasification technologies can effectively and efficiently convert a wide variety of carbonaceous feedstocks (coal, petcoke, resids, biomass, etc.) into syngas, which predominantly contains carbon monoxide and hydrogen. Unfortunately, the impurities present in these carbonaceous feedstocks are converted to gaseous contaminants such as H2S, COS, HCl, NH3, alkali macromolecules and heavy metal compounds (such as Hg) during the gasification process. Removal of these contaminants using conventional processes is thermally inefficient and capital intensive. This research and development effort is focused on investigation of modular processes for removal of sulfur, chlorine, nitrogen and mercury compounds from syngas at elevated temperature and pressures at significantly lower costs than conventional technologies.

  7. Increasing the strength of metallurgical coke by adding modified petroleum coke to the coking batch

    Energy Technology Data Exchange (ETDEWEB)

    M.I. Stukov; V.S. Zagainov; Y.B. Kukolev; N.S. Andreichikov; P.V. Shtark; A.V. Vishnyakov; V.A. Antonova; S.N. Soboleva [Eastern Coal-Chemistry Institute, Yekaterinburg (Russian Federation)

    2009-08-15

    Box-coking data show the possibility of increasing the yield and strength of metallurgical coke by introducing a coking additive in the batch. Specifically, this additive is a product of slow coking of heavy petroleum residues, characterized by excellent thermoplastic properties: clinkering properties and plastic temperature range. A Russian patent has been obtained for the coking additive.

  8. Textile Dry Cleaning Using Carbon Dioxide: Process, Apparatus and Mechanical Action

    OpenAIRE

    Sutanto, S.

    2014-01-01

    Fabrics that are sensitive to water, may wrinkle or shrink when washed in regular washing machines and are usually cleaned by professional dry cleaners. Dry cleaning is a process of removing soils from substrate, in this case textile, using a non-aqueous solvent. The most common solvent in conventional dry cleaning is perchloroethylene (PER). Despite its satisfactory cleaning performance, PER has several drawbacks. One approach is to develop an alternative solvent for PER. CO2 is chosen in th...

  9. Advances towards a Clean Hydrometallurgical Process for Chromite

    Directory of Open Access Journals (Sweden)

    Bo Zhang

    2016-01-01

    Full Text Available Because of the acute toxicity of Cr(VI-bearing substances, the pollution problem caused by chromite process residue has become a worldwide concern. In the view of relevant studies, the technologies based on the alkali treatment cannot fundamentally resolve the pollution problem, because the oxidation of Cr(III to Cr(VI is unavoidable during chromite decomposition. In contrast, the oxidation of Cr(III to Cr(VI can be controlled by the sulfuric acid treatment of chromite, and the Cr(VI pollution can be eliminated from the original source of production. Many research studies focusing on the resolutions of the key obstacles hindering the development of the sulfuric acid treatment process have been carried out, and significant progress has been achieved. In this study, a clean hydrometallurgical process without the generation of hexavalent chromium is demonstrated. First, the chromite was decomposed and leached by sulfuric acid solution in the presence of an oxidant. Then, iron was hydrothermally removed from the acid solution as the precipitate of jarosite. Finally, chromium salts were obtained by adjusting the basicity of the solution, separation and drying. With the aim of realizing industrialization, future research emphasis on the development of the sulfuric acid treatment process is proposed in this study.

  10. The effect of blast furnace coke quality on the possibility of its use

    OpenAIRE

    Konstanciak, A.

    2013-01-01

    In the paper behavior of the blast-furnace coke in the high temperature was presented. Comparative analysis of the chemical composition of the blast-furnace coke and the heat treatment of it were done. Coefficients M10 and M40 with the thermo-abrasiveness for chosen cokes were compared. The influence of ash content of the coke on the blast-furnace bed permeability was defined. Usefulness of the coke to blast-furnace process was also defined.

  11. Expectation for coke quality seen from recent blast furnace operation in Japan

    Energy Technology Data Exchange (ETDEWEB)

    Ogata, I.; Ichida, M. [Nippon Steel Corp. Ltd, Futtsu (Japan)

    2004-09-01

    The coke quality requested for the stable operation of a large-scale blast furnace under high production and low coke rate in the future is arranged based on a past finding concerning relation between the coke quality and the blast furnace operation analysis. And an expectation for next generation coke-making process (SCOPE21) which has the function to enable the above-mentioned coke quality and a necessary requirement are described.

  12. Coke Oven Gas Based Methanol Production Capacity Reached 1.2 Mt/a in China

    Institute of Scientific and Technical Information of China (English)

    2008-01-01

    @@ Coke oven gas is one of the main byproducts of coke chemicals industry.One ton of coke formed can generate 430 m3of coke oven gas.Adoption of appropriate chemical processing method can convert methane contained in the coke oven gas into CO that can be further converted into methanol.It is learned that currently China has constructed and commissioned ten projects for manufacture of methanol fromcoke oven gas with the total production capacity reaching 1.2 Mt/a methanol.More than twenty coke gas-to-methanol units are under construction or in the stage of project design with their overall production capacity reaching nearly 3.0 Mt/a methanol.Relevant experts have indicated that the enterprises provided with coke production lines are capable of constructing coke gas-to-methanol projects to realize coproduction of coke and methanol while utilizing their own coke gas resources.

  13. The coke drum thermal kinetic effects

    Energy Technology Data Exchange (ETDEWEB)

    Aldescu, Maria M.; Romero, Sim; Larson, Mel [KBC Advanced Technologies plc, Surrey (United Kingdom)

    2012-07-01

    The coke drum thermal kinetic dynamics fundamentally affect the coker unit yields as well as the coke product properties and unit reliability. In the drum the thermal cracking and polymerization or condensation reactions take place in a semi-batch environment. Understanding the fundamentals of the foaming kinetics that occur in the coke drums is key to avoiding a foam-over that could result in a unit shutdown for several months. Although the most dynamic changes with time occur during drum filling, other dynamics of the coker process will be discussed as well. KBC has contributed towards uncovering and modelling the complexities of heavy oil thermal dynamics. (author)

  14. Technical Progress of China's Delayed Coking Technology

    Institute of Scientific and Technical Information of China (English)

    Zhang Lixin; Li Hejie

    2005-01-01

    This article introduces the recent advances of China in the fields of process technology of delayed coking, enlarged equipment size, hydraulic decoking, automatic control and environmental protection. By the end of 2004 the total capacity of delayed coking units in China had reached 37.24Mt/a with the maximum coke drum diameter equating to 9.4 m. This article also presents the investment in delayed cokers and the current production status while pointing out the existing problems and future development trends.

  15. 单种焦煤结焦性能及其混配性研究%Coking capacity and coking compatibility of coking coals

    Institute of Scientific and Technical Information of China (English)

    项茹; 宋子逵; 薛改凤; 鲍俊芳

    2012-01-01

    The quality and coking capacity of 5 coking coals from different mines were analyzed and compared, and coal blend coking experiment was conducted. The results show, although the coking capacity of the coals doesn't differ much, their process indexes and coking microstructures are remarkably different. During blending and coking, if the coking has abundant plastometers with high fluxion and expansion and more coarse coking grains, its coking compatibility with different coals will be good and the coke quality will also be high, and vice versa.%对5种不同矿点的焦煤进行煤质分析和单种煤结焦性能比较,并进行配煤炼焦试验研究.结果表明,尽管单种焦煤的结焦性能接近,但其工艺性质及成焦显微结构存在较大差异.在配煤炼焦中,胶质体含量丰富、胶质体的流变性和膨胀性高、成焦粗粒镶嵌结构多的焦煤,与不同炼焦煤的混配性强,所得焦炭质量较优.

  16. Advanced treatment of biologically pretreated coking wastewater by intensified zero-valent iron process (IZVI) combined with anaerobic filter and biological aerated filter (AF/BAF)

    Institute of Scientific and Technical Information of China (English)

    潘碌亭; 韩悦; 吴锦峰

    2015-01-01

    Experiments were conducted to investigate the behavior of the sequential system of intensified zero-valent iron process (IZVI) and anaerobic filter and biological aerated filter (AF/BAF) reactors for advanced treatment of biologically pretreated coking wastewater. Particular attention was paid to the performance of the integrated system for the removal of chemical oxygen demand (COD), ammonia nitrogen (NH3-N) and total nitrogen (TN). The average removal efficiencies of COD, NH3-N and TN were 76.28%, 96.76% and 59.97%, with the average effluent mass concentrations of 56, 0.53 and 18.83 mg/L, respectively, reaching the first grade of the national discharge standard. Moreover, the results of gas chromatography/mass spectrum (GC/MS) and gel permeation chromatography (GPC) analysis demonstrated that the refractory organic compounds with high relative molecular mass were partly removed in IZVI process by the function of oxidation-reduction, flocculation and adsorption which could also enhance the biodegradability of the system effluent. The removal efficiencies of NH3-N and TN were achieved mainly in the subsequent AF/BAF reactors by nitrification and denitrification. Overall, the results obtained show that the application of IZVI in combination with AF/BAF is a promising technology for advanced treatment of biologically pretreated coking wastewater.

  17. Coke oven gas desulfurization: at Republic Steel's New Coking Facility, Warren, OH

    Energy Technology Data Exchange (ETDEWEB)

    Boak, S.C.; Prucha, D.G.; Turic, H.L.

    1981-01-01

    Our performance test indicates that the Sulfiban process is an effective method for removing H/sub 2/S from coke-oven gas. The process is able to handle variations in coke-oven gas flow and composition. Continuing efforts are underway to maintain optimum desulfurization conditions while trying to reduce waste production and MEA consumption. The problems which have prevented us from operating continuously have given us a better understanding of the process. This has contributed to better plant operations and greater equipment reliability for us to obtain continuous coke-oven gas desulfurization. 2 figures, 1 table.

  18. Fundamentals of Delayed Coking Joint Industry Project

    Energy Technology Data Exchange (ETDEWEB)

    Michael Volk; Keith Wisecarver

    2003-09-26

    is 2,937,439 barrels/calendar day. These cokers produce 154,607 tons of coke per day and delayed coking accounts for 88% of the world capacity. The delayed coking charge capacity in the United States is 1,787,860 b/cd. Despite its wide commercial use, only relatively few contractors and refiners are truly knowledgeable in delayed-coking design, so that this process carries with it a ''black art'' connotation. Until recently, the expected yield from cokers was determined by a simple laboratory test on the feedstock. As a result of Tulsa University's prior related research, a process model was developed that with additional work could be used to optimize existing delayed cokers over a wide range of potential feedstocks and operating conditions. The objectives of this research program are to: utilize the current micro, batch and pilot unit facilities at The University of Tulsa to enhance the understanding of the coking process; conduct additional micro and pilot unit tests with new and in-house resids and recycles to make current optimization models more robust; conduct focused kinetic experiments to enhance the furnace tube model and to enhance liquid production while minimizing sulfur in the products; conduct detailed foaming studies to optimize the process and minimize process upsets; quantify the parameters that affect coke morphology; and to utilize the knowledge gained from the experimental and modeling studies to enhance the computer programs developed in the previous JIP for optimization of the coking process. These refined computer models will then be tested against refinery data provided by the member companies. Novel concepts will also be explored for hydrogen sulfide removal of furnace gases as well as gas injection studies to reduce over-cracking.

  19. Fundamentals of Delayed Coking Joint Industry Project

    Energy Technology Data Exchange (ETDEWEB)

    Michael Volk; Keith Wisecarver

    2004-09-26

    is 2,937,439 barrels/calendar day. These cokers produce 154,607 tons of coke per day and delayed coking accounts for 88% of the world capacity. The delayed coking charge capacity in the United States is 1,787,860 b/cd. Despite its wide commercial use, only relatively few contractors and refiners are truly knowledgeable in delayed-coking design, so that this process carries with it a ''black art'' connotation. Until recently, the expected yield from cokers was determined by a simple laboratory test on the feedstock. As a result of Tulsa University's prior related research, a process model was developed that with additional work could be used to optimize existing delayed cokers over a wide range of potential feedstocks and operating conditions. The objectives of this research program are to: utilize the current micro, batch and pilot unit facilities at The University of Tulsa to enhance the understanding of the coking process; conduct additional micro and pilot unit tests with new and in-house resids and recycles to make current optimization models more robust; conduct focused kinetic experiments to enhance the furnace tube model and to enhance liquid production while minimizing sulfur in the products; conduct detailed foaming studies to optimize the process and minimize process upsets; quantify the parameters that affect coke morphology; and to utilize the knowledge gained from the experimental and modeling studies to enhance the computer programs developed in the previous JIP for optimization of the coking process. These refined computer models will then be tested against refinery data provided by the member companies. Novel concepts will also be explored for hydrogen sulfide removal of furnace gases as well as gas injection studies to reduce over-cracking.

  20. Material compatibility and corrosion control of the KWU chemical cleaning process

    International Nuclear Information System (INIS)

    The concentrations of salt impurities within the deposits on the tube sheet and in the tube to tube-support-plate crevices can induce a variety of corrosion mechanisms on steam generator tubes. One of the most effective ways of counteracting corrosion mechanisms and thus of improving steam generator performance is to clean the steam generators and keep them in a clean condition. As shown by field results chemical cleaning is a way of removing hazardous deposits from steam generators. All available chemical cleaning processes use inhibitors to control the corrosion except the KWU chemical cleaning process. In this article the corrosion control technique of KWU Chemical Cleaning Process without using conventional inhibitors will be explained and the state of the field experience with respect to material compatibility will be presented. (author). 4 figs., 1 tab., 8 refs

  1. Effect of cleaning process on the combustion characteristics of two different rank coals

    Energy Technology Data Exchange (ETDEWEB)

    Kok, M.V.; Hicyilmaz, C.; Ozbas, K.E. [Middle East Technical University, Ankara (Turkey). Dept. of Mining Engineering

    2001-12-01

    In this research, thermogravimetry (TG/DTG) was used to determine the combustion characteristics of two different rank coals (Tuncbilek and Afsin Elbistan) before and after cleaning process. Applying sink-float process cleaned raw coal samples, and optimum-separating densities for each sample was determined using the criteria of 'degree of washability'. The results indicated that coal cleaning was very effective on Tuncbilek sample due to its high rank. TG/DTG analysis of raw and cleaned samples indicated different reaction regions occurring at different temperature intervals. Easy combustibility and long-lasting combustion were the distinctive effects of coal cleaning on raw coals. Kinetic analysis of the samples showed that clean coals require lower activation energies to initiate the combustion process than raw coals. 14 refs., 6 figs., 10 tabs.

  2. Fatigue behaviour of coke drum materials under thermal-mechanical cyclic loading

    Directory of Open Access Journals (Sweden)

    Jie Chen

    2014-01-01

    Full Text Available Coke drums are vertical pressure vessels used in the delayed coking process in petroleum refineries. Significant temperature variation during the delayed coking process causes damage in coke drums in the form of bulging and cracking. There were some studies on the fatigue life estimation for the coke drums, but most of them were based on strain-fatigue life curves at constant temperatures, which do not consider simultaneous cyclic temperature and mechanical loading conditions. In this study, a fatigue testing system is successfully developed to allow performing thermal-mechanical fatigue (TMF test similar to the coke drum loading condition. Two commonly used base and one clad materials of coke drums are then experimentally investigated. In addition, a comparative study between isothermal and TMF lives of these materials is conducted. The experimental findings lead to better understanding of the damage mechanisms occurring in coke drums and more accurate prediction of fatigue life of coke drum materials.

  3. Tests of an environmental and personnel safe cleaning process for BNL accelerator and storage ring components

    International Nuclear Information System (INIS)

    A large measure of the successful operation of the National Synchrotron Light Source (NSLS) at Brookhaven National Laboratory (BNL) for over a decade can be attributed to the cleaning of its UHV components during and after construction. A new UHV cleaning process, which had to be environmentally and personnel safe, was needed to replace the harsh, unfriendly process which was still in use. Dow Advanced Cleaning Systems was contracted to develop a replacement process without the use of harsh chemicals and which must clean vacuum surfaces as well as the existing process. Acceptance of the replacement process was primarily based on Photon Stimulated Desorption (PSD) measurements of beam tube samples run on NSLS beam line U10B. One meter long beam tube samples were fabricated from aluminum, 304 stainless steel and oxygen free copper. Initially, coupon samples were cleaned and passed preliminary testing for the proposed process. Next, beam tube samples of each material were cleaned, and the PSD measured on beam line U10B using white light with a critical energy of 487 ev. Prior to cleaning, the samples were contaminated with a mixture of cutting oils, lubricants, vacuum oils and vacuum grease. The contaminated samples were then baked. Samples of each material were also cleaned with the existing process after the same preparation. Beam tube samples were exposed to between 1022 and 1023 photons per meter for a PSD measurement. Desorption yields for H2, CO, CO2, CH4 and H2O are reported for both the existing cleaning and for the replacement cleaning process. Preliminary data, residual gas scans, and PSD results are given and discussed. The new process is also compared with new cleaning methods developed in other laboratories

  4. Generic methods for coke oven gas desulphurisation

    Energy Technology Data Exchange (ETDEWEB)

    Wilfried Seyfferth; Rainer Dittmer; Holger Thielert [ThyssenKrupp EnCoke GmbH, Bochum (Germany)

    2004-07-01

    The presentation gives an overview of the most common desulphurisation processes suitable for coke oven gas. Dry oxidative processes mentioned include the iron oxide and the zinc oxide process; wet oxidative processes outlined are the Stretford, Perox, Takahax, Thylox, Fumaks and LoCat; and neutralizaiton or absorption/stripping processes described are the Sulfiban, CYCLASULF, VACASULF and Soda Lye scrubbing processes. 22 figs.

  5. Proposal of a novel multifunctional energy system for cogeneration of coke, hydrogen, and power - article no. 052001

    Energy Technology Data Exchange (ETDEWEB)

    Jin, H.G.; Sun, S.; Han, W.; Gao, L. [Chinese Academy of Sciences, Beijing (China)

    2009-09-15

    This paper proposes a novel multifunctional energy system (MES), which cogenerates coke, hydrogen, and power, through the use of coal and coke oven gas (COG). In this system, a new type of coke oven, firing coal instead of COG as heating resource for coking, is adopted. The COG rich in H{sub 2} is sent to a pressure swing adsorption (PSA) unit to separate about 80% of hydrogen first, and then the PSA purge gas is fed to a combined cycle as fuel. The new system combines the chemical processes and power generation system, along with the integration of chemical conversion and thermal energy utilization. In this manner, both the chemical energy of fuel and thermal energy can be used more effectively. With the same inputs of fuel and the same output of coking heat, the new system can produce about 65% more hydrogen than that of individual systems. As a result, the thermal efficiency of the new system is about 70%, and the exergy efficiency is about 66%. Compared with individual systems, the primary energy saving ratio can reach as high as 12.5%. Based on the graphical exergy analyses, we disclose that the integration of synthetic utilization of COG and coal plays a significant role in decreasing the exergy destruction of the MES system. The promising results obtained may lead to a clean coal technology that will utilize COG and coal more efficiently and economically.

  6. Techniques for laser spectroscopy of actinide elements: developments in the clean-up process

    International Nuclear Information System (INIS)

    Configuration of an efficient laser clean-up process requires a large amount of basic atomic data provided by careful high resolution spectroscopic experiments involving one or several lasers, both pulsed and cw. Efforts in developing such sources for high resolution spectroscopy in the context of the clean-up process are discussed

  7. Electro-membrane processes for flue gas cleaning

    Energy Technology Data Exchange (ETDEWEB)

    Larsen, T. F.

    1997-12-31

    , the energy consumption for regeneration of 250 kJ/mole SO{sub 2}, at a current density of 150 mA/Cm{sup 2} and 200 kJ/mole SO{sub 2}, at a current density of 50 mA/cm{sup 2}, have been achieved. This may be compared to the energy consumption of about 1200 kJ/mole SO{sub 2} for the conventional process (steam stripping) for regeneration. The problems arising from fouling of membranes due to the presence of impurities in the liquid have also been studied. These studies have then been used for evaluating the requirement for cleaning of liquids before regeneration. (EG) EFP-94. 95 refs.

  8. Coke Formation During Hydrocarbons Pyrolysis. Part Two: Methane Thermal Cracking Formation de coke pendant la pyrolyse des hydrocarbures. Deuxième partie : pyrolyse du méthane

    OpenAIRE

    Billaud F.; Broutin P.; Busson C.; Gueret C.

    2006-01-01

    Part one of this article dealt with coking in a steam cracking furnace. In this process, coke deposition is a very complex phenomenon due to the number of parameters involved. Nevertheless, for this process, coke deposition is a secondary reaction which does not affect steam cracking yields. It is completely different for methane thermal cracking. Coke is one of the main products of this reaction. Part two of this article deals with coke deposition on the walls of the reactors used for methan...

  9. Process of cleaning oil spills and the like

    International Nuclear Information System (INIS)

    A process of cleaning spills of toxic or hazardous materials such as oil, antifreeze, gasoline, and the like from bodies of water, garage floors, roadways and the like, comprising spraying unbonded shredded fiberglass blowing wool composition particles onto the spill, absorbing the spill into the shredded fiberglass blowing wool composition particles, and removing the soaked shredded fiberglass blowing wool composition particles and the spill absorbed therein. An absorbent composition for absorbing spills of toxic or hazardous materials such as oil, antifreeze, gasoline, and like, comprising shredded fiberglass blowing wool particles, and means for absorbing the spill and for stiffening the co-position so that the composition fights against being compressed so that less of the absorbed spill escapes from the composition when it is being removed from the spill, said means including cork particles dispersed in with the fiberglass blowing wool particles. An absorbent sock for absorbing or containing a spill of toxic or hazardous materials such as oil, antifreeze, gasoline, and the like, comprising a hollow tube, said tube being permeable to the toxic or hazardous materials and being made of nylon or polypropylene, and unbonded, shredded fiberglass blowing wool composition particles enclosed in the tube. Apparatus for controlling an oil slick on the surface of water, comprising a craft for traversing the slick, a supply of fiberglass blowing wool composition particles stored on the craft in position for being dispersed, shredding means on the craft for shredding the fiberglass blowing wool particles to form unbonded, shredded fiberglass blowing wool particles, and dispensing means on the craft for dispensing the unbonded, shredded fiberglass blowing wool particles onto the slick

  10. Process and device for cleaning furnace exhaust gas in a vitrification plant

    International Nuclear Information System (INIS)

    The furnace exhaust gas produced during vitrification is cleaned of carried over dust particles in an exhaust gas cleaning stage using a washing liquid. In order to achieve a simplified process for dosing and exhaust gas cleaning, radioactive fission product solution is taken from the feed container as the washing liquid and is transported to the head of the exhaust gas cleaning stage. The fission product solution noting as washing liquid is returned to the feed container after passing through the exhaust gas cleaning stage. The furnace exhaust gas of the vitrification plant is taken through the exhaust gas cleaning stage in counterflow. The invention also concerns a device to carry out this process. (orig./HP)

  11. Development of environmentally conscious cleaning process for leadless chip carrier assemblies. Final report

    Energy Technology Data Exchange (ETDEWEB)

    Adams, B.E.

    1995-04-01

    A cross-functional team of process, product, quality, material, and design lab engineers was assembled to develop an environmentally friendly cleaning process for leadless chip carrier assemblies (LCCAs). Using flush and filter testing, Auger surface analysis, GC-Mass spectrophotometry, production yield results, and electrical testing results over an extended testing period, the team developed an aqueous cleaning process for LCCAs. The aqueous process replaced the Freon vapor degreasing/ultrasonic rinse process.

  12. 甲醇制烯烃 SAPO-34催化剂的积炭失活%Deactivation by Coke of SAPO-34 Catalyst in Methanol to Olefins Process

    Institute of Scientific and Technical Information of China (English)

    吴秀章

    2014-01-01

    综述了在甲醇催化转化制低碳烯烃(MTO)过程中,SAPO-34分子筛催化剂积炭失活的影响。催化剂积炭失活后,会严重影响 MTO 反应的转化率和选择性。在较高反应温度下,焦炭主要是芳烃类物质,催化剂上的积炭,是起反应活性的物种在强酸性位上继续反应生成的,焦炭会覆盖强酸中心并会堵塞微孔而产生扩散限制。SAPO-34分子筛的强酸中心及密度、晶粒尺寸,是影响催化剂积炭失活速率的主要催化剂参数,而反应温度、空速及稀释剂,是影响催化剂应用过程中积炭失活速率的主要操作变量。%Deactivation by coke of SAPO-34 catalyst and its effect on reaction in methanol conversion to light olefins process were reviewed. Serious coking deactivation affects the conversion and light olefin selectivity of MTO process. At high reaction temperature, the coke is mainly composed of aromatics. The coke is formed on the Br-nsted acid site from active precursor, the coke covers the Br-nsted acid site, blocks the micropores and leads to diffusion limit. The Br-nsted acid site and its density, the size of SAPO-34 crystal particles are the main parameters which affect the coking rate. The reaction temperature, space velocity and diluent are the main operation variables.

  13. Study on the Combined Process of Ebullated Bed Residue Hydroprocessing and Coking%沸腾床渣油加氢-焦化组合工艺探讨

    Institute of Scientific and Technical Information of China (English)

    刘建锟; 杨涛; 方向晨; 蒋立敬

    2015-01-01

    Technical test and economic comparison on two technical routes of the combination process of ebullated bed hydrotreating with coking and direct coking were done to choose suitable for inferior residue processing .The results showed that the impurity of the product from ebullated bed residue hydroprocessing of inferior residue feedstock was significantly reduced .Compared with inferior residue feedstock ,hydroprocessed vacuum residue was greatly improved ,whose impurity content was significantly reduced .The S ,Ni ,V mass fractions of hydroprocessed residue were decreased by 90% ,95% ,99% ,respectively ,under reaction temperature of base+5/base+ 5 and base LHSV .Compared with coking process ,the combination of ebullated bed and coking could process inferior residue feedstock ,from which the total liquid volume was increased by 13.57% and the ability to increase production of high value-added products was significantly improved ,thus the economic efficiency was greatly enhanced . Meanwhile , the combination process has obvious advantages of improving stability ,wide adaptability of feedstock and flexible process ,w hich is the preferred option to improve crude oil resource utilization .%针对劣质渣油加工,分别采用沸腾床渣油加氢-焦化组合工艺与单独焦化工艺两种技术路线进行探讨,以选择其适合的加工技术路线。结果表明,劣质渣油原料经沸腾床加氢,产品杂质含量显著降低。在双反应器温度基准+5/基准+5、基准空速条件下,劣质渣油加氢产品的S、N i、V质量分数分别下降了90%、95%、99%。与劣质渣油原料相比,沸腾床加氢减压渣油的性质得到极大改善。与单独焦化工艺相比,采用组合工艺加工劣质渣油,总液体产率提高了13.57%,增产高附加值产品的能力明显提升,从而大幅度提高经济效益。同时,该组合工艺具有改善油品稳定性、原料适应性广、工艺灵活等明显

  14. Cleaning and Processing RSS measurements for Location Fingerprinting

    DEFF Research Database (Denmark)

    Kjærgaard, Mikkel Baun

    2007-01-01

    Handling variations in sampled Received Signal Strength (RSS) is neassary for achieving robust location fingerprinting (LF). Current research has only proposed limited system-specific models for how to handle the cleaning of RSS variations. However, this paper propose a novel model for both...

  15. SMALLHOLDER COFFEE PROCESSING DESIGN USING WET TECHNOLOGY BASED ON CLEAN PRODUCTION

    OpenAIRE

    RIZAL SYARIEF; ELIDA NOVITA; ERLIZA NOOR; SRI MULATO

    2012-01-01

    Wet processing for red coffee berry is intended to improve smallholder coffee quality despite produce wastewater that can pollute the environment. In order to minimize and prevent wastewater generated from processing, then it should be designed coffee processing based on water minimization as part of clean production. The purpose of this study is to design smallholder coffee processing using wet method based on clean production that can provide added value and environmental friendly. This stu...

  16. Application of response surface methodology to the chemical cleaning process of ultrafiltration membrane☆

    Institute of Scientific and Technical Information of China (English)

    Caihong Wang; Aishu Wei; Hao Wu; Fangshu Qu; Weixiong Chen; Heng Liang; Guibai Li

    2016-01-01

    A numerical model was established to predict and optimise the chemical cleaning process of Polyvinylidene Fluo-ride (PVDF) Ultrafiltration (UF) membranes with the results from the experiment that applied the Response Sur-face Method (RSM) and Central Composite Design (CCD). The factors considered in the experimental design were sodium hydroxide (NaOH) concentration, sodium hypochlorite concentration (NaClO), citric acid concentration and cleaning duration. The interactions between the factors were investigated with the numerical model. Humic acid (20 mg·L−1) was used as the model foulant, and chemical enhanced backflush (CEB) was employed to sim-ulate the chemical cleaning process. The concentrations of sodium hydroxide, sodium hypochlorite, citric acid and cleaning duration tested during the experiments were in the range of 0.1%–0.3%, 100–300 mg·L−1, 1%–3%and 0.5–1.5 h, respectively. Among the variables, the sodium hypochlorite concentration and the cleaning dura-tion showed a positive relationship involving the increased efficiency of the chemical cleaning. The chemical cleaning efficiency was hardly improved with increasing concentrations of sodium hydroxide. However, the data was sharply decreased when at a low level of sodium hydroxide concentration. In total, 54 sets of cleaning schemes with 80%to 100%cleaning efficiency were observed with the RSM model after calibration.

  17. The importance of cleaning for the overall results of processing endoscopes.

    Science.gov (United States)

    Martiny, H; Floss, H; Zühlsdorf, B

    2004-04-01

    Reprocessing comprises three steps: cleaning, disinfection and-if required-sterilisation. While the extents of disinfection and of sterilisation are quantitatively defined, there are only imprecise (qualitative) definitions of cleaning. There are two main reasons for accurate cleaning. First organic and inorganic materials that remain on inner and outer surfaces will interfere with the efficacy of the disinfectants. In case of endoscopes this will lead to channel blockages; they remain undisinfected. Second the bioburden found on endoscopes after use can be very high. Data available demonstrate that a bacterial burden of up to 10(9)cfu/endoscope channel can be expected. Therefore it is necessary to perform a thorough cleaning. Studies using endoscopes showed a reduction in microbial counts by a factor of approximately 10(4) by cleaning (manual and mechanical). Therefore in 2001 the German Society of Hospital Hygiene (DGKH) specified its requirements and recommendations for determining cleaning efficacy separately from those for disinfection. Cleaning and disinfecting can be done manually or mechanically, but it seems impossible to validate manual processes. However our studies in two different washer-disinfectors (WD) showed differences in cleaning efficacy. The tested cleaning processes showed different efficacies. Not all cleaning processes showed better results than water alone with regard to visible cleanliness and to a microbiological reduction E. faecium. Our results show that the evaluation of cleanliness exclusively by visible inspection is not sufficient, particular for the lumens of endoscopes. The results also show that a cleaning process may be very effective also in reducing micro-organisms present. PMID:15110118

  18. 7 CFR 201.33 - Seed in bulk or large quantities; seed for cleaning or processing.

    Science.gov (United States)

    2010-01-01

    ... 7 Agriculture 3 2010-01-01 2010-01-01 false Seed in bulk or large quantities; seed for cleaning or... (CONTINUED) FEDERAL SEED ACT FEDERAL SEED ACT REGULATIONS Labeling in General § 201.33 Seed in bulk or large quantities; seed for cleaning or processing. (a) In the case of seed in bulk, the information required...

  19. Textile Dry Cleaning Using Carbon Dioxide: Process, Apparatus and Mechanical Action

    NARCIS (Netherlands)

    Sutanto, S.

    2014-01-01

    Fabrics that are sensitive to water, may wrinkle or shrink when washed in regular washing machines and are usually cleaned by professional dry cleaners. Dry cleaning is a process of removing soils from substrate, in this case textile, using a non-aqueous solvent. The most common solvent in conventio

  20. Removal of organic compounds and trace metals from oil sands process-affected water using zero valent iron enhanced by petroleum coke.

    Science.gov (United States)

    Pourrezaei, Parastoo; Alpatova, Alla; Khosravi, Kambiz; Drzewicz, Przemysław; Chen, Yuan; Chelme-Ayala, Pamela; Gamal El-Din, Mohamed

    2014-06-15

    The oil production generates large volumes of oil sands process-affected water (OSPW), referring to the water that has been in contact with oil sands or released from tailings deposits. There are concerns about the environmental impacts of the release of OSPW because of its toxicity. Zero valent iron alone (ZVI) and in combination with petroleum coke (CZVI) were investigated as environmentally friendly treatment processes for the removal of naphthenic acids (NAs), acid-extractable fraction (AEF), fluorophore organic compounds, and trace metals from OSPW. While the application of 25 g/L ZVI to OSPW resulted in 58.4% removal of NAs in the presence of oxygen, the addition of 25 g petroleum coke (PC) as an electron conductor enhanced the NAs removal up to 90.9%. The increase in ZVI concentration enhanced the removals of NAs, AEF, and fluorophore compounds from OSPW. It was suggested that the electrons generated from the oxidation of ZVI were transferred to oxygen, resulting in the production of hydroxyl radicals and oxidation of NAs. When OSPW was de-oxygenated, the NAs removal decreased to 17.5% and 65.4% during treatment with ZVI and CZVI, respectively. The removal of metals in ZVI samples was similar to that obtained during CZVI treatment. Although an increase in ZVI concentration did not enhance the removal of metals, their concentrations effectively decreased at all ZVI loadings. The Microtox(®) bioassay with Vibrio fischeri showed a decrease in the toxicity of ZVI- and CZVI-treated OSPW. The results obtained in this study showed that the application of ZVI in combination with PC is a promising technology for OSPW treatment. PMID:24681364

  1. The identification of dangerously coking coals

    Energy Technology Data Exchange (ETDEWEB)

    Barriocanal, C.; Patrick, J.W.; Walker, P.A. [Loughborough Univ. of Technology, Leicestershire (United Kingdom)] [and others

    1995-12-31

    When coals are carbonised in slot-type ovens, layers of plastic coal are formed parallel to the oven walls and move progressively inwards eventually meeting at the oven centre. It is within these plastic layers that the principal processes which result in particulate coal being converted into porous, fused coke take place. For some coals, usually having volatile matter contents between 17 and 25wt% (dry, ash-free basis), these processes are accompanied by the generation of measurable gas pressures within the plastic layers which attain maximum levels when the two layers meet at the oven centre. These pressures are transmitted through the coke to the oven walls, causing damage if sufficiently high. Other coals, similar in chemical analysis and swelling properties, can be carbonised with impunity. The technical aspects of the coking pressure phenomenon are well known. However, the fundamental processes involved in the generation of internal gas pressures are not fully understood. Thus, before being used in blends for commercial coke production, potentially dangerous coals are tested by carbonising upwards of 180kg charges in moveable-wall ovens and measuring directly the pressures exerted on the walls. Clearly, it would be helpful if dangerously coking coals could be identified from laboratory tests. Preliminary findings of a laboratory study designed to gain further insight into coking pressure development are presented in this paper. Internal gas pressures have been ascribed to volatiles trapped within either the plastic envelope or the plastic layer implying an overlap of the temperature ranges of volatile release and fluidity. An attempts to assess this view using, initially, thermogravimetric analysis and Gieseler plastometry and, later, a coking bomb are described, the results being related to internal gas pressures measured in a 1.5kg double-wall oven.

  2. Functionalization of Petroleum Coke-Derived Carbon for Synergistically Enhanced Capacitive Performance

    Science.gov (United States)

    Zhang, Yan; Li, Xuejin; Huang, Jufeng; Xing, Wei; Yan, Zifeng

    2016-03-01

    Petroleum coke is a valuable and potential source for clean energy storage if it could be modified legitimately and facilely. In the present study, porous carbon with high surface area and abundant oxygen-containing groups was prepared from petroleum coke by chemical activation and modification processes. The as-prepared carbon exhibits a high surface area (1129 m2 · g-1) and stable micrographic structure. It presents a high specific capacitance and excellent rate performance in KOH electrolyte. Even at an ultrahigh current density of 50 A · g-1, the specific capacitance of the prepared carbon can still reach up to an unprecedented value of 261 F · g-1 with a superhigh retention rate of 81 %. In addition, the energy density of this material in aqueous electrolyte can be as high as 13.9 Wh · kg-1. The high energy density and excellent rate performance ensure its prosperous application in high-power energy storage system.

  3. Progress in the desulfurization of coke oven gas and utilization of H[sub 2]S - Still Otto's SOLOX process

    Energy Technology Data Exchange (ETDEWEB)

    Tippmer, K. (Thyssen Still Otto Anlagentechnik, GmbH, Bochum (Germany))

    1994-01-01

    The SOLOX process developed by Still Otto to remove sulfur from coke oven gas down to a content of less than 2 ppm of H[sub 2]S is essentially based on practical experience gained from the construction of plants operating according to the well-known Stretford process. Economic as well as ecological problems with secondary pollutant formation from H[sub 2]S, HCN and O[sub 2] which are notorious in liquid-phase oxidation processes could be eliminated by providing for a combination with salt cracking processes operating according to the liquid-phase hydrolysis principle, with the gaseous hydrolysis products H[sub 2]S, NH[sub 3] and CO[sub 2] being returned to the raw gas and the regenerated solution recycled to the absorption process. The desulfurization process can either be located downstream of the NH[sub 3] BTX removal unit which is the typical arrangement or, as a modified solution, upstream of it. A cost-benefit analysis has revealed the advantages of the new process over the AS circulation and vacuum-carbonate processes both from an economic as well as ecological view point. 21 refs., 11 figs., 6 tabs.

  4. Chemical Cleaning Process for Porable Water Distrubution Pipe Systems

    OpenAIRE

    ECT Team, Purdue

    2007-01-01

    Aging potable water distribution pipe systems are becoming a major concern throughout the world. Deterioration of water quality and service as a result of micro biological tuberculation and corrosion continues to increase. Major costs for replacement or rehabilitation of distribution systems are being faced by most communities. The chemical cleaning solution is an organic oxide scavenger which is mixed with a predetermined quantity of muriatic acid and circulated through an isolated section o...

  5. Pace studying worldwide coke production

    International Nuclear Information System (INIS)

    Pace Consultants Inc., Houston, has started a multiclient study of world-wide petroleum coke production, examining environmental initiatives and eventually forecasting prices of fuel grade coke. Pace expects coker expansions, increased operating severity, and reduced cycle times to boost coke supply to more than 50 million metric tons/year in 2000, compared with 39.7 million metric tons in 1992. Increased supply and tightened environmental rules in countries consuming large amounts of petroleum coke will be the main factors affecting coke markets. The paper discusses coke quality and the Japanese market

  6. Identifying optimal cleaning cycles for heat exchangers subject to fouling and ageing

    International Nuclear Information System (INIS)

    Fouling of heat exchangers causes reduced heat transfer and other penalties. Regular cleaning represents one widely used fouling mitigation strategy, where the schedule of cleaning actions can be optimised to minimise the cost of fouling. This paper investigates, for the first time, the situation where there are two cleaning methods available so that the mode of cleaning has to be selected as well as the cleaning interval. Ageing is assumed to convert the initial deposit, labelled 'gel', into a harder and more conductive form, labelled 'coke', which cannot be removed by one of the cleaning methods. The second method can remove both the gel layer and the coke layer, but costs more and requires the unit to be off-line longer for cleaning. Experimental data demonstrating the effects of ageing are presented. The industrial application is the comparison of cleaning-in-place methods with off-line mechanical cleaning. A process model is constructed for an isolated counter-current heat exchanger subject to fouling, where ageing is described by a simple two-layer model. Solutions generated by an NLP-based approach prove to be superior to a simpler heuristic. A series of case studies demonstrate that combinations of chemical and mechanical cleaning can be superior to mechanical cleaning alone for certain combinations of parameters.

  7. Intelligent Collaboration Control of Gas Collection Pipe Pressure in Coke Oven Processes%焦炉集气管压力的智能协调控制

    Institute of Scientific and Technical Information of China (English)

    叶鲁彬; 王屹; 杨建波

    2014-01-01

    设计了一种集气管压力的智能协调控制方案,解决焦炉集气管压力之间耦合严重,稳定性较差,极易出现压力振荡现象。综合考虑多集气管及风机、回流的特性,集气管翻板阀采用双模式PID算法,风机或回流阀进行整体吸力的协调控制,同时引入了振荡检测机制,并对压力振荡进行抑制。该控制方案的效果已在焦化企业现场得到了实践验证,并在多个现场应用。%In the gas collection process of coke ovens, the pipes have high coupling relations, which result in the unstableness of the pressure. The pressure oscillation phenomena are frequently reported in practical productions. This paper proposed an intelligent collaboration control solution, which take the characteristics of gas collection pipes, fan and the recycle pipe into consideration. Dual-mode PID algorithm is utilized in the gas collection pipe pressure control formulation and the fan speed and recycle valve are manipulated to keep the entire lfow power. Pressure oscillation detection is introduced here to prevent severe lfuctuation of the pipe pressure. The proposed method has been validated and is widely used in the coke production plants.

  8. 焦炉气的生产与利用及工艺螺杆压缩机的选择%The Production and Utilization of Coke Oven Gas and Selection of Process Screw Compressor

    Institute of Scientific and Technical Information of China (English)

    曾跃波; 易柳峰; 李志才

    2014-01-01

    阐述了炼焦过程中煤炭隔绝空气高温干馏出来的气体产物———焦炉煤气的生产与利用现状;阐述了焦炉煤气的传统及新型的利用途径,着重介绍了利用焦炉煤气制LNG的甲烷化和净化分离工艺及制氢新工艺、该利用途径带来的环境及经济效益、以及引入螺杆压缩机所带来的优势;并对制甲醇等工艺过程特点、市场供需形势做了简要叙述,并对焦炉气未来几年的发展空间作了预测。%The gas products out of coking coal in the process of air isolation and high-temperature dry distillation-coke oven gas and the production and utilization were introduced.The traditional and a new utilization way of the coke oven gas were expounded, focused on narrating the methanation and purification separation technology utilization of coke oven gas for LNG and new technology for hydrogen production, environmental and economic benefits generated from the utilization way.The advantages benefited by introducing process screw compressor into the technology, briefly elaborated the process characteristics of producting methanol process and the situation of market supply and demand, and the development space of coke oven gas in the next few years.

  9. Cleaning of liquid LLW from decontamination processes using semipermeable membranes

    International Nuclear Information System (INIS)

    Of the three processes, which have been used extensively for liquid radioactive waste purification, evaporation and ion exchange are costly and flocculation gives a low degree of purification. By comparison to that, reverse osmosis offers intermediate purification at reasonable cost. Present research is examining the potential of using a membrane filtration system for the removal of dissolved radionuclides, but chemical treatment showed as necessary to convert soluble radionuclides, organic traces and metals to insoluble, filterable species. Liquid wastes within a CANDU station are segregated into normal and low-activity waste streams. The normal-activity waste includes wastes from the laboratories, laundries, some service-building drains, upgrade drains, and decontamination center. The drains from the reactor building, the heavy-water area, the spent-fuel pool, and the resin storage area are also directed to this normal activity wastes from showers and building drains in areas of the service building that would not normally be contaminated. The aqueous liquid wastes from the decontamination center and the other collected wastes from the chemical drain system are currently treated by the membrane plant. Generally, the liquid waste streams are effectively volume-reduced by a combination of continuous crossflow microfiltration (MF), spiral wound reverse osmosis (SWRO) and tubular reverse osmosis membrane technologies. Backwash chemical cleaning wastes from the membrane plant are further volume-reduced by evaporation. The concentrate from the membrane plant is ultimately immobilized with bitumen. The ability of the MF/SWRO technology to remove impurities non-selectively makes it suitable for the treatment of radioactive effluents from operating nuclear plants, with proper membrane selection, feed characterization, system configuration and system chemistry control. The choice of polysulfonate material for membrane was based on the high flow rates achievable with this

  10. Coke Deposition and Smoke Formation in Turbojet Engines

    Science.gov (United States)

    Hibbard, R. R.; Wear, J. D.

    1956-01-01

    , structure, and chemical composition of the soft coke in the dome and (2) the hard deposits on the liner are similar to petroleum coke and may result from the liquid-phase thermal cracking of the fuel. During the early development period of jet engines, it was noted that the excessive coke deposits and exhaust smoke were generally obtained when fuel-oil-type fuels were used. Engines using gasoline-type fuels were relatively free from the deposits and smoke. These results indicated that some type of quality control would be needed in fuel specifications. Also noted was the effect of engine operating conditions on coke deposition. It is possible that, even with a clean-burning fuel, an excessive amount of coke could be formed at some operating conditions. In this case, combustor redesign could possibly reduce the coke to a tolerable level. This chapter is a summary of the various coke-deposition and exhaust-smoke problems connected- with the turbojet combustor. Included are (1) the effect of coke deposition on combustor life or durability and performance; (2) the effect of combustor design, operating conditions, inlet variables, and fuel characteristics on coke deposition; (3) elimination of coke deposits; (4) the effect of operating conditions and fuel characteristics on formation of exhaust smoke; and (5) various bench test methods proposed for determining and controlling fuel quality.

  11. Utilization of semi-coke for energy production

    International Nuclear Information System (INIS)

    The review describes some problems and possibilities associated with the spent shale from the Kiviter process. Kiviter AS in cooperation with the Finnish power company Imatraan Voima OY is doing a project study on power generation from semi-coke. The main alternative is to burn the semi-coke in a high-pressured fluidized bed

  12. TREATMENT TANK CORROSION STUDIES FOR THE ENHANCED CHEMICAL CLEANING PROCESS

    Energy Technology Data Exchange (ETDEWEB)

    Wiersma, B.

    2011-08-24

    Radioactive waste is stored in high level waste tanks on the Savannah River Site (SRS). Savannah River Remediation (SRR) is aggressively seeking to close the non-compliant Type I and II waste tanks. The removal of sludge (i.e., metal oxide) heels from the tank is the final stage in the waste removal process. The Enhanced Chemical Cleaning (ECC) process is being developed and investigated by SRR to aid in Savannah River Site (SRS) High-Level Waste (HLW) as an option for sludge heel removal. Corrosion rate data for carbon steel exposed to the ECC treatment tank environment was obtained to evaluate the degree of corrosion that occurs. These tests were also designed to determine the effect of various environmental variables such as temperature, agitation and sludge slurry type on the corrosion behavior of carbon steel. Coupon tests were performed to estimate the corrosion rate during the ECC process, as well as determine any susceptibility to localized corrosion. Electrochemical studies were performed to develop a better understanding of the corrosion mechanism. The tests were performed in 1 wt.% and 2.5 wt.% oxalic acid with HM and PUREX sludge simulants. The following results and conclusions were made based on this testing: (1) In 1 wt.% oxalic acid with a sludge simulant, carbon steel corroded at a rate of less than 25 mpy within the temperature and agitation levels of the test. No susceptibility to localized corrosion was observed. (2) In 2.5 wt.% oxalic acid with a sludge simulant, the carbon steel corrosion rates ranged between 15 and 88 mpy. The most severe corrosion was observed at 75 C in the HM/2.5 wt.% oxalic acid simulant. Pitting and general corrosion increased with the agitation level at this condition. No pitting and lower general corrosion rates were observed with the PUREX/2.5 wt.% oxalic acid simulant. The electrochemical and coupon tests both indicated that carbon steel is more susceptible to localized corrosion in the HM/oxalic acid environment than

  13. Fine coal cleaning via the micro-mag process

    Science.gov (United States)

    Klima, Mark S.; Maronde, Carl P.; Killmeyer, Richard P.

    1991-01-01

    A method of cleaning particulate coal which is fed with a dense medium slurry as an inlet feed to a cyclone separator. The coal particle size distribution is in the range of from about 37 microns to about 600 microns. The dense medium comprises water and ferromagnetic particles that have a relative density in the range of from about 4.0 to about 7.0. The ferromagnetic particles of the dense medium have particle sizes of less than about 15 microns and at least a majority of the particle sizes are less than about 5 microns. In the cyclone, the particulate coal and dense-medium slurry is separated into a low gravity product stream and a high gravity produce stream wherein the differential in relative density between the two streams is not greater than about 0.2. The low gravity and high gravity streams are treated to recover the ferromagnetic particles therefrom.

  14. Clean-up and disposal process of polluted sediments from urban rivers

    Institute of Scientific and Technical Information of China (English)

    2001-01-01

    In this paper, the discussion is concentrated on the properties of the polluted sediments and the combination of clean-up and disposal process for the upper layer heavily polluted sediments with good flowability. Based on the systematic analyses of various clean-up processes, a suitable engineering process has been evaluated and recommended. The process has been applied to the river reclamation in Yangpu District of Shanghai metropolis. An improved centrifuge is used for dewatering the dredged sludge,which plays an important role in the combination of clean-up and disposal process. The assessment of the engineering process shows its environmental and technical economy feasibility, which is much better than that of traditional dredging-disposal processes.

  15. Advanced treatment of residual nitrogen from biologically treated coke effluent by a microalga-mediated process using volatile fatty acids (VFAs) under stepwise mixotrophic conditions.

    Science.gov (United States)

    Ryu, Byung-Gon; Kim, Woong; Heo, Sung-Woon; Kim, Donghyun; Choi, Gang-Guk; Yang, Ji-Won

    2015-09-01

    This work describes the development of a microalga-mediated process for simultaneous removal of residual ammonium nitrogen (NH4(+)-N) and production of lipids from biologically treated coke effluent. Four species of green algae were tested using a sequential mixotrophic process. In the first phase-CO2-supplied mixotrophic condition-all microalgae assimilated NH4(+)-N with no evident inhibition. In second phase-volatile fatty acids (VFAs)-supplied mixotrophic condition-removal rates of NH4(+)-N and biomass significantly increased. Among the microalgae used, Arctic Chlorella sp. ArM0029B had the highest rate of NH4(+)-N removal (0.97 mg/L/h) and fatty acid production (24.9 mg/L/d) which were 3.6- and 2.1-fold higher than those observed under the CO2-supplied mixotrophic condition. Redundancy analysis (RDA) indicated that acetate and butyrate were decisive factors for increasing NH4(+)-N removal and fatty acid production. These results demonstrate that microalgae can be used in a sequential process for treatment of residual nitrogen after initial treatment of activated sludge. PMID:25881553

  16. The plasma etching methods for minimizing mask CD variation by cleaning process

    Science.gov (United States)

    Shin, Hyun D.; Jeong, Soo K.; Jung, Ho Y.; Kim, Sang P.; Yim, Dong G.

    2012-11-01

    There has been a growing demand for more precise Mask CD MTT (Critical Dimension Mean to Target) control by shrinking the semiconductor device. Generally, The CD MTT is determined by patterning process such as writing, develop, and etch. But, additional CD MTT variation often occurs by cleaning process after patterning process. As a result, it is important to preserve the CD MTT for minimizing CD variation by cleaning process. The cleaning process of photomask is becoming more critical for 32nm node and below because the size of defect and SRAF pattern is in the same range. In order to achieve high first cleaning pass yields, intensive cleaning method depending on media not physical force is still essential to photomask manufacturing and these cleaning processes bring about considerable CD MTT change. Therefore, it is necessary to increase the durability of MoSi material of attenuated HTPSM (Half Tone Phase Shift Mask) by the new surface treatment method. In this study, we presented the plasma etching technique for Cr strip etch in the 2nd process of the attenuated HTPSM for minimizing CD variation by cleaning process. Diverse dry etching processes are investigated to improve the durability of the MoSi patterns. In order to evaluate the surface modification of the MoSi film, surface compositions are analyzed by XPS (X-ray Photoelectron Spectroscopy), TOF-SIMS (Time of Flight Secondary Ion Mass Spectrometry), and EELS (Electron Energy Loss Spectroscopy). The variation of CD MTT and optical properties are also evaluated by CD SEM and AIMS (Aerial Image Measurement System), respectively. The XPS analysis shows that sidewall passivation films are formed during the main etch process and then modified at the over etch step and additional in-situ O2 plasma treatment. The concentration of the MoO3 is increased when over etch step and in-situ O2 plasma treatment are added. The difference of CD shift between initial measurement and 2nd measurement after cleaning process

  17. PWR steam generator chemical cleaning process testing in model steam generators

    International Nuclear Information System (INIS)

    Corrosion related problems in PWR power plant steam generators have caused high maintenance costs, increased radiation exposure to plant personnel, and reduced unit availability. Two cleaning methods were investigated for their ability to clean deposits from steam generators thereby increasing the integrity of the steam generators and reducing personnel radiation exposure, due to reduced maintenance. First, an on-line chemical cleaning process (Chelant Addition) was tested for its ability to prevent corrosion product buildup in a steam generator. Second, an off-line dilute chemical cleaning process was tested to evaluate its ability to remove corrosion product deposits and leave minimal waste for disposal. These two processes were tested in model steam generators which simulated the operating conditions of a typical full size steam generator. Six model steam generators (MSG) were fabricated and qualified for their ability to reproduce denting at tube support plates. The results of six chemical cleaning tests and the post-cleaning destructive metallurgical evaluation of two of the model steam generators are reported

  18. Coke yield and heat transfer in reaction of liquid-solid agglomerates of Athabasca vacuum residue

    Energy Technology Data Exchange (ETDEWEB)

    Ali, M.; Courtney, M.; Boddez, L.; Gray, M. [Alberta Univ., Edmonton, AB (Canada). Dept. of Chemical and Materials Engineering

    2010-02-15

    Delayed coking and fluid-bed coking are the most common commercial processes used by the petroleum industry for the thermal conversion of vacuum residues into petroleum distillate products. This paper presented the results of an experimental study of coke yield at long reaction times from agglomerates of coke particles and Athabasca vacuum residue (AVR). The ultimate coke yield was determined for a range of agglomerate thicknesses, liquid concentrations and reaction temperatures. The agglomerates were heated on Curie-point alloy strips in an induction furnace at 503 and 530 degrees C until all toluene-soluble material was converted. A simple heat transfer model was used to describe the temperature profile within the agglomerates. Coke yield results from agglomerates were compared to the coke yield results from reacting thin films of vacuum residue. The average coke yield from the agglomerates was 23 per cent, while the coke yield from thin films of 20 {mu}m thickness was 11 per cent, which supports the role of mass transfer in coke formation reactions. The ultimate coke yield was insensitive to vacuum residue concentration, agglomerate size, and reaction temperature. According to control experiments on thin films of liquid at different heating rates, the temperature-time history has little effect on the ultimata coke yield. 13 refs., 2 tabs., 10 figs.

  19. Texture of cokes in relation to parameters of coal and coke

    OpenAIRE

    Pěgřimočová, J.

    2013-01-01

    The article presents a proposal of the simplified classification of textures of coke and the relationship between the texture parameters of coke both coal, from which the coke was made, and properties of the coke.

  20. Correlation between particle removal and shock-wave dynamics in the laser shock cleaning process

    International Nuclear Information System (INIS)

    It has been shown that the laser shock cleaning (LSC) method is effective for eliminating micron- and submicron-scale particulates from solid surfaces. In the LSC process, a high-power laser pulse induces optical breakdown of the ambient gas close to the solid surface to be cleaned and the subsequently-created shock wave followed by a high-speed flow stream detaches the particles. Therefore, there should be a strong correlation between the dynamics of the shock wave and the cleaning performance. In this work, experimental analyses are conducted to measure the cleaning performance using micron-sized alumina particles attached to a silicon surface. The experimental data showing the particle-removal performance are compared with the results of the dynamics of the laser-induced shock waves, leading to a simple model for particle removal by the LSC scheme in the continuum-flow regime

  1. The effect of additive chemicals on the viscosity of coal-petroleum coke-water slurry fuel for a gasification process

    Energy Technology Data Exchange (ETDEWEB)

    Yoon, S.J.; Choi, Y.C.; Lee, J.G. [Korean Institute of Energy Research, Taejon (Republic of Korea)

    2009-09-15

    As a preliminary study for the gasification of an anthracite and petroleum coke mixture, viscosity was measured at various temperatures (20-50{sup o}C, slurry concentrations (60-70 wt%) and additive amounts (0-0.8 wt%) by using an LV-II type viscometer. In addition, four types of different additives, sodium naphthalene sulfonate, poly(methyl methacrylate), polypropylene and a polypropylene glycol based additive, were applied to Korean anthracite, petroleum coke and mixtures of these materials, and the viscosity data were compared. Viscosity dependency values for coal, anthracite, bituminous and sub-bituminous coal, were compared, and it was found that a high content of moisture and particularly ash increases CWS viscosity. The four types of additives tested in this research can effectively diminish the viscosity of coal and especially petroleum coke-water slurry by more than 70% to 95%, respectively. Moreover, the sodium naphthalene sulfonate-based additive reduced the viscosity of coal and petroleum coke-water slurry best, especially at concentrations in excess of 65 wt%. Based on these results, highly loaded slurry created by mixing anthracite and petroleum coke with additives was achieved.

  2. Report of clean out and flushing of UO3 Plant processing equipment: Revision 1

    International Nuclear Information System (INIS)

    The UO3 Plant went through a clean out leading to the deactivation of the facility. This clean out consisted of three phases. Phase 1 consisted of the removal of residual process material and the deactivation of most process equipment and instrumentation. Phase 2 consisted of the fixing or removal of contamination so storm water processing would be no longer required. Phase 3 consisted of the remaining activities that had to be completed before the facility was turned over to the Surplus Facility Program. Since the activities of Phase 2 and 3 were closely related, these two phases were worked simultaneously. The first part of this document summarizes the Phase 1 clean out procedures and their results. Phase 1 was completed on February 28, 1994. The second part summarizes the Phase 2/3 clean out procedures and their results. Phase 2/3 was completed before December 31, 1994. Because tanks and equipment were flushed simultaneously or in a specific sequence, the clean out processes are discussed per workplan

  3. Fundamentals of Delayed Coking Joint Industry Project

    Energy Technology Data Exchange (ETDEWEB)

    Michael Volk Jr; Keith Wisecarver

    2005-10-01

    is 2,937,439 barrels/calendar day. These cokers produce 154,607 tons of coke per day and delayed coking accounts for 88% of the world capacity. The delayed coking charge capacity in the United States is 1,787,860 b/cd. Despite its wide commercial use, only relatively few contractors and refiners are truly knowledgeable in delayed-coking design, so that this process carries with it a ''black art'' connotation. Until recently, the expected yield from cokers was determined by a simple laboratory test on the feedstock. As a result of Tulsa University's prior related research, a process model was developed that with additional work could be used to optimize existing delayed cokers over a wide range of potential feedstocks and operating conditions. The objectives of this research program are to: utilize the current micro, batch and pilot unit facilities at The University of Tulsa to enhance the understanding of the coking process; conduct additional micro and pilot unit tests with new and in-house resids and recycles to make current optimization models more robust; conduct focused kinetic experiments to enhance the furnace tube model and to enhance liquid production while minimizing sulfur in the products; conduct detailed foaming studies to optimize the process and minimize process upsets; quantify the parameters that affect coke morphology; and to utilize the knowledge gained from the experimental and modeling studies to enhance the computer programs developed in the previous JIP for optimization of the coking process. These refined computer models will then be tested against refinery data provided by the member companies. Novel concepts will also be explored for hydrogen sulfide removal of furnace gases as well as gas injection studies to reduce over-cracking. The following deliverables are scheduled from the two projects of the three-year JIP: (1) A novel method for enhancing liquid yields from delayed cokers and data that provide insight as to

  4. Using ultrafine particles from a coal washing plant in metallurgical coke production

    Directory of Open Access Journals (Sweden)

    Jesús Manuel Gutierrez Bernal

    2011-01-01

    Full Text Available Blending ultrafine particles from a coal washing plant was studied for coke production by briquetting using 6%w coal tar as binder. The ultrafine coal particles were characterised and a pilot coking test was made in a Koppers’ furnace. Coke quality was evaluated by proximate analysis, stability (micum 10 and micum 40, coke reactivity index (CRI with CO2 and the coke’s mechanical strength after reaction with carbon dioxide (CSR index. Briquetting results showed that was possible to obtain coke having 19.0 % CRI and 75.6% CSR, these being the characteristics required in metallurgical processes.

  5. The effect of blast furnace coke quality on the possibility of its use

    Directory of Open Access Journals (Sweden)

    A. Konstanciak

    2013-04-01

    Full Text Available In the paper behavior of the blast-furnace coke in the high temperature was presented. Comparative analysis of the chemical composition of the blast-furnace coke and the heat treatment of it were done. Coefficients M10 and M40 with the thermo-abrasiveness for chosen cokes were compared. The influence of ash content of the coke on the blast-furnace bed permeability was defined. Usefulness of the coke to blast-furnace process was also defined.

  6. Catalytic Processes for Clean Hydrogen Production from Hydrocarbons

    OpenAIRE

    ÖNSAN, Zeynep İlsen

    2007-01-01

    Conversion of hydrocarbon fuels to hydrogen with a high degree of purity acceptable for fuel cell operation presents interesting challenges for the design of new selective catalysts and catalytic processes. Natural gas, LPG, gasoline, and diesel are regarded as promising hydrocarbon fuels. Methanol has received attention despite its toxicity, and ethanol has recently become of interest as a much less toxic and renewable resource. Selective catalytic processes considered for commerci...

  7. Development of Statistical Process Control Methodology for an Environmentally Compliant Surface Cleaning Process in a Bonding Laboratory

    Science.gov (United States)

    Hutchens, Dale E.; Doan, Patrick A.; Boothe, Richard E.

    1997-01-01

    Bonding labs at both MSFC and the northern Utah production plant prepare bond test specimens which simulate or witness the production of NASA's Reusable Solid Rocket Motor (RSRM). The current process for preparing the bonding surfaces employs 1,1,1-trichloroethane vapor degreasing, which simulates the current RSRM process. Government regulations (e.g., the 1990 Amendments to the Clean Air Act) have mandated a production phase-out of a number of ozone depleting compounds (ODC) including 1,1,1-trichloroethane. In order to comply with these regulations, the RSRM Program is qualifying a spray-in-air (SIA) precision cleaning process using Brulin 1990, an aqueous blend of surfactants. Accordingly, surface preparation prior to bonding process simulation test specimens must reflect the new production cleaning process. The Bonding Lab Statistical Process Control (SPC) program monitors the progress of the lab and its capabilities, as well as certifies the bonding technicians, by periodically preparing D6AC steel tensile adhesion panels with EA-91 3NA epoxy adhesive using a standardized process. SPC methods are then used to ensure the process is statistically in control, thus producing reliable data for bonding studies, and identify any problems which might develop. Since the specimen cleaning process is being changed, new SPC limits must be established. This report summarizes side-by-side testing of D6AC steel tensile adhesion witness panels and tapered double cantilevered beams (TDCBs) using both the current baseline vapor degreasing process and a lab-scale spray-in-air process. A Proceco 26 inches Typhoon dishwasher cleaned both tensile adhesion witness panels and TDCBs in a process which simulates the new production process. The tests were performed six times during 1995, subsequent statistical analysis of the data established new upper control limits (UCL) and lower control limits (LCL). The data also demonstrated that the new process was equivalent to the vapor

  8. COMPARING STUDY OF BLENDING PREHEATING MODIFIED COAL COKING AND STAMPING COKING FOR DONGSHEN COAL

    Institute of Scientific and Technical Information of China (English)

    伍林; 尹学琼; 魏贤勇; 宗志敏; 陈清如

    1999-01-01

    The compaison of the properties of coke of three coking methods is introduced. The mechanical properties and high temperature reactivity of coke blending preheating modified Dongshen coal are improved obviously than those of normal coke, and achieve or exceed that of stamping coke. This method shews more ability of expending coking coal resources.

  9. On-site raw gas cut-off during the shut down of Baosteel phase I coke ovens

    Institute of Scientific and Technical Information of China (English)

    ZHOU Haizhong

    2015-01-01

    The preparation and implementation of raw coke oven gas cut-off,which was the key process involved with shutting down the Baosteel phase I coke ovens,were investigated,and the main technical points and countermeasures are presented.

  10. The TEES process cleans waste and produces energy

    International Nuclear Information System (INIS)

    A gasification system is under development that can be used with most types of wet organic wastes. The system operates at 350 degrees C and 205 atm using a liquid water phase as the processing medium. Since a pressurized system is used, the wet waste can be fed as a solution or slurry to the reactor without drying. Through the development of catalysts, a useful processing system has been produced. The system has utility both for direct conversion of high-moisture biomass to fuel gas or as a wastewater cleanup system for wet organic wastes including unconverted biomass from bioconversion processes. By the use of this system >99% conversions of organic waste to medium-Btu fuel gas can be achieved

  11. Programmed heating of coke ovens for increased coke size

    Energy Technology Data Exchange (ETDEWEB)

    Jenkins, D.R.; Mahoney, M.R. [University of Newcastle, Callaghan, NSW (Australia)

    2010-11-15

    Large, uniform sized coke is desirable for blast furnace use. It has previously been shown that the coke oven flue temperature in the first few hours of coking is a key determinant of coke size. In this paper, the authors present a new programmed heating approach, which is called pulsed heating, aiming to increase coke mean size at a given average flue temperature. The approach takes into account the charging sequence in coke oven batteries and the authors demonstrate how existing operating practice can be modified in batteries with suitable heating systems to achieve the desired heating programme. A mathematical model of fissure formation provides a prediction of the increase in coke mean size using pulsed heating, compared with standard heating. Pilot scale experiments have also been performed to validate the modelling approach. The results of the modelling indicate that the mean coke size can be increased by several millimetres in some cases, although results from the pilot scale show that pulsed heating increases coke size, but by a smaller amount than that predicted by the model. The potential advantages and limitations of pulsed heating are discussed, as well as opportunities for further investigation of the approach.

  12. Process for cleaning waste gases containing hydrogen fluoride and fluorine

    International Nuclear Information System (INIS)

    The waste gases are taken into an aqueous solution of uranium(IV) sulphate, where insoluble uranium tetrafluoride hydrate is formed. This can be returned to the manufacturing process for uranium hexafluoride. The uranyl sulphate which is also formed is best reduced to uranium(IV) where the reduction need not be complete, because of the excess of uranium(IV). (PW)

  13. Advanced catalytic plasma exhaust clean-up process for ITER-EDA

    Energy Technology Data Exchange (ETDEWEB)

    Glugla, M. [Kernforschungszentrum Karlsruhe, Inst. fuer Radiochemie (Germany); Penzhorn, R.D. [Kernforschungszentrum Karlsruhe, Inst. fuer Radiochemie (Germany); Hermann, P. [Kernforschungszentrum Karlsruhe, Inst. fuer Radiochemie (Germany); Ache, H.J. [Kernforschungszentrum Karlsruhe, Inst. fuer Radiochemie (Germany)

    1995-12-31

    A new catalyst reactor (PERMCAT) has been developed to further improve the catalytic conversion / permeation based plasma exhaust clean-up process realized in the facility CAPRICE at the Tritium Laboratory Karlsruhe (TLK). The reactor directly combines a nickel catalyst with permeation tubes and removes residual amounts of tritium from tritiated species by isotopic swamping with hydrogen. Succesful integration of such a unit into the CAPRICE catalytic clean-up approach could lead to a fully continuous process and bring about a considerable reduction in non-recoverable tritium. (orig.).

  14. Advanced catalytic plasma exhaust clean-up process for ITER-EDA

    International Nuclear Information System (INIS)

    A new catalyst reactor (PERMCAT) has been developed to further improve the catalytic conversion / permeation based plasma exhaust clean-up process realized in the facility CAPRICE at the Tritium Laboratory Karlsruhe (TLK). The reactor directly combines a nickel catalyst with permeation tubes and removes residual amounts of tritium from tritiated species by isotopic swamping with hydrogen. Succesful integration of such a unit into the CAPRICE catalytic clean-up approach could lead to a fully continuous process and bring about a considerable reduction in non-recoverable tritium. (orig.)

  15. Effects of Additives on Sulfur Transformation, Crystallite Structure and Properties of Coke during Coking of High-sulfur Coal

    Institute of Scientific and Technical Information of China (English)

    Sheng-fu ZHANG; Liang-ying WEN; Kun WANG; Chong ZOU; Jian XU

    2015-01-01

    High-sulfur coal, as an alternative coal source, has a relatively high proportion in coal reserves. However, the feature of high sulfur content, which can cause environmental pollution and poor quality of molten iron, restrains its utilization in coking industry. Coking experiments of high-sulfur coal with Fe2O3, La2O3 and CaO as additives were carried out in order to ifx the sulfur in coke. The effects of additives on sulfur distribution, crystallite structure, surface morphology and properties of coke were inves-tigated. The results indicate that CaO can be used as sulfur-ifxing agent in coking process, and CaS is the main mineralogical phase of the sulfur-contained mineral constituents in coke. Fe2O3 and La2O3 facilitate the conversion of CaO to CaS. The additives mainly inlfuence the crystallite height and the average interlayer spacingd002 of coke. The addition of La2O3 increases the value of the crys-tallite heightwhile the addition of CaO and Fe2O3 decreases it. CaO leads the pores of coke to increase with its physical action and agglomerating characteristic. Fe2O3and C can form (Fe,C), resulting in the pulverization and erosion of the pore wall. La2O3 makes the coke surface become more compact and thinner. The reactivity of coke increases with the decrease of crystallite height and crystallite layer number.

  16. DMT - Areva's steam generator maintenance cleaning process concept and experiences

    International Nuclear Information System (INIS)

    Steam generators (SGs) are one of the key components for plant performance and plant availability of nuclear power plants. Depending on numerous factors (e.g. material concept, water chemistry, operational procedures) a certain amount of metal oxides and impurities are transported into the SG's via the feed water. Accumulation of these deposits is intrinsic during the operation of steam generators in PWRs. In order to maintain the integrity or to maintain or regain the performance of the steam generators, chemical cleaning is an essential part of the asset management. Recently the industry moves from curative (removing all SG deposits with one chemical application) cleanings to preventive (i.e. maintenance - removal of a portion of the SG deposits with one chemical application) cleanings. The intention of such preventive cleanings is to maintain the deposit inventory on a low level or even better to reduce the deposit inventory by repeated applications. Preventive cleanings remove only a part of the sludge inventory during each application. Nevertheless such cleanings still need to be efficient and most of all it is mandatory that the corrosion is very low - not only to minimize steam generator base metal corrosion but also to increase the efficiency of the cleaning. The AREVA developed proprietary Deposit Minimization Treatment (DMT) technology uses a different chemistry than EDTA. The technical advantage provided by DMT's different chemistry, besides the innocuousness towards Ni-alloys and stainless steels, is its self-inhibiting property. The in situ formation of a protective layer on the carbon steel surfaces limits the average carbon steel corrosion during a typical chemical cleaning campaign to values far below 10 μm. Due to this very low carbon steel corrosion, less than 5 % of the dissolved iron originates from SG base metal corrosion, while this portion can be more than 30 % in a comparable uninhibited EDTA solution. The DMT process protective

  17. Investigation of the impact of cleaning on the adhesive bond and the process implications

    Energy Technology Data Exchange (ETDEWEB)

    EMERSON,JOHN A.; GUESS,TOMMY R.; ADKINS,CAROL L. JONES; CURRO,JOHN G.; REEDY JR.,EARL DAVID; LOPEZ,EDWIN P.; LEMKE,PAUL A.

    2000-05-01

    While surface cleaning is the most common process step in DOE manufacturing operations, the link between a successful adhesive bond and the surface clean performed before adhesion is not well understood. An innovative approach that combines computer modeling expertise, fracture mechanics understanding, and cleaning experience to address how to achieve a good adhesive bond is discussed here to develop a capability that would result in reduced cleaning development time and testing, improved bonds, improved manufacturability, and even an understanding that leads to improved aging. A simulation modeling technique, polymer reference interaction site model applied near wall (Wall PRISM), provided the capability to include contaminants on the surface. Calculations determined an approximately 8% reduction in the work of adhesion for 1% by weight of ethanol contamination on the structure of a silicone adhesive near a surface. The demonstration of repeatable coatings and quantitative analysis of the surface for deposition of controlled amounts of contamination (hexadecane and mineral oil) was based on three deposition methods. The effect of the cleaning process used on interfacial toughness was determined. The measured interfacial toughness of samples with a Brulin cleaned sandblasted aluminum surface was found to be {approximately} 15% greater than that with a TCE cleaned aluminum surface. The sensitivity of measured fracture toughness to various test conditions determined that both interfacial toughness and interface corner toughness depended strongly on surface roughness. The work of adhesion value for silicone/silicone interface was determined by a contact mechanics technique known as the JKR method. Correlation with fracture data has allowed a better understanding between interfacial fracture parameters and surface energy.

  18. Intensification of the process of cleaning ballast water

    Energy Technology Data Exchange (ETDEWEB)

    Stepaneks, L.

    1983-01-01

    A large part of the waste water at offshore bulk plants is oil-containing ballast water of tankers. Its volume can reach 40-50% of their tonnage. In order to purify this water, mainly two-stage plans are currently used with mechanical methods in the first stage and physical mechanical in the second. In this case the concentration of petroleum products in the purified waste water is 15-20 mg/1. The need to improve the efficiency of the active treatment complexes (TC) results in considerable increase in cost of TC construction. In order to intensify the process of purification of waste water, the Institute of Biology of the Southern Seas of the Ukrainian SSR Academy of Sciences has conducted laboratory studies to investigate the filtering activity of Black Sea mussles, a study was made of the viability of filtering organisms under different conditions of contamination. Studies of these processes made it possible to develop a biological method for purification of oil-containing waste water with the use of marine organisms. Based on many years of practical operation of structures to purify oil-containing ballast water of tankers at the active treatment complex of the offshore bulk plant ''Sheskharis'' and studies to improve the operating efficiency of the TC, a plan was developed for purifying the oil-containing ballast water of tankers with the use of the biological method.

  19. Causes Leading to Formation of Shot Cokes and Measures for Its Prevention in Super Viscous Oil Delayed Coking Unit

    Institute of Scientific and Technical Information of China (English)

    Chen Chunmao; Zhang Feng; Yan Guangxu; Guo Shaohui

    2007-01-01

    Shot cokes are frequently formed in the delayed coking unit treating the super viscous oil at PetroChina's Liaohe Petrochemical Company. Considerable work has been carried out to avoid the formation of shot cokes. The test results obtained have shown that the property of super viscous oil has played a key role in the formation of shot cokes. After adjusting and optimizing the process indices the operating regime of the delayed coking unit at a throughput of 118t/h of the super viscous oil is specified as follows: a reaction temperature of 498-502℃, a reaction pressure of 0.17-0.25 MPa, a recycle ratio of 0.5-0.6 and a fractionation tower bottom temperature of 355-365 ℃. In the meantime,the delayed coking process has adopted measures to enhance pre-fractionation of the feedstock to rationally remove light fractions and maintain a steady gas velocity in order to avoid the formation of shot cokes.

  20. Effect of yttrium on the coking behavior of Fe-based superalloy in heavy hydrocarbon

    International Nuclear Information System (INIS)

    Graphical abstract: Compared with bare specimen (a), specimen doped with yttrium (b) shows the elimination of the intergranular coking behavior of Fe-based superalloy and changes the coke morphology. - Highlights: • Effect of Y on the coking behavior of Fe-based superalloy was studied. • The alloy doped with Y exhibits the better coking and carbonizing resistance. • Y doped in the alloy eliminates the intergranular coking and carbonization. - Abstract: Effect of the rare earth element yttrium on the coking behavior of Fe-based superalloy has been studied. The coking process of Fe-based superalloy during dodecane pyrolysis includes three stages – incubation period, coke protrusions growing and graphite layer stacking. Fe-based superalloy with yttrium addition exhibits the better coking and carburization resistance. The reason is that Y doped in Fe-based superalloy eliminates the intergranular coking and carburization by forming yttrium oxides to inhibit the aggregation of Cr2O3 at the grain boundary in initial period of coking behavior, thus internal Cr2O3 layer forms and effectively blocks the permeation of outer graphite

  1. Tests of an environmental and personnel safe cleaning process for Brookhaven National Laboratory accelerator and storage ring components

    International Nuclear Information System (INIS)

    A large measure of the successful operation of the National Synchrotron Light Source (NSLS) at Brookhaven National Laboratory (BNL) for over a decade can be attributed to the cleaning of its ultrahigh vacuum (UHV) components during and after construction. A new UHV cleaning process, which has to be environmentally and personnel safe, is needed to replace the harsh, unfriendly process which is still in use. Dow Advanced Cleaning Systems was contracted to develop a replacement process without the use of harsh chemicals and which must clean vacuum surfaces as well as the existing process. Acceptance of the replacement process was primarily based on photon stimulated desorption (PSD) measurements of beam tube samples run on NSLS beam line U10B. One meter long beam tube samples were fabricated from aluminum, 304 stainless steel, and oxygen-free copper. Initially, coupon samples were cleaned and passed preliminary testing for the proposed process. Next, beam tube samples of each material were cleaned, and the PSD measured on beam line U10B using white light with a critical energy of 487 eV. Prior to cleaning, the samples were contaminated with a mixture of cutting oils, lubricants, vacuum oils, and vacuum grease. The contaminated samples were then baked. Samples of each material were also cleaned with the existing process after the same preparation. Beam tube samples were exposed to between 1022 and 1023 photons per meter for a PSD measurement. Desorption yields for H2, CO, CO2, CH4, and H2O are reported for both the existing cleaning and for the replacement cleaning process. Preliminary data, residual gas scans, and PSD results are given and discussed. The new process is also compared with new cleaning methods developed in other laboratories. After modification, the new UHV cleaning process was accepted by BNL

  2. Analysis of Application of CMC Technology in Coal Coking Process%煤调湿技术在焦化工序中的应用分析

    Institute of Scientific and Technical Information of China (English)

    何传超; 罗国民

    2013-01-01

    SGIS is located in southern China,the water in coal blending for coking is too high for years,which leads to a decrease of coke production,a waste of gas resources,and instability of the coke oven and thus a reduction of its service life.Based on the actual situation of coking in SGIS and through the data comparison before and after the use of the coal moisture control technology (CMC),this paper suggests adopting the CMC technology,which can not only achieve environmental protection,also create considerable economic benefits for SGIS every year.%韶钢地处华南地区,长年炼焦配煤的含水量过高,这不仅降低了焦炭的产量,浪费煤气资源,还降低焦炉的稳定性,影响焦炉的寿命.根据韶钢焦化的实际情况,建议采用煤调湿技术,通过前后对比数据说明:采用煤调湿技术,不仅可以达到环保目的,每年还可创造可观的经济效益.

  3. Femtosecond pulses cleaning by transient-grating process in Kerr-optical media

    Institute of Scientific and Technical Information of China (English)

    Jun Liu; Kotaro Okamura; Yuichiro Kida; Takayoshi Kobayashi

    2011-01-01

    We use a transient-grating (TG) process in a Kerr bulk medium to clean a femtosecond laser pulse. Using the technique, the temporal contrast of the generated TG signal is improved by more than two orders of magnitude in comparison with the incident pulse in a 0.5-mm-thick fused silica plate. The laser spectrum is smoothed and broadened, and the pulse duration is shortened simultaneously. We expect to extend this technique to a clean pulse with broadband spectral bandwidth at a wide spectral range because it is a phase-matched process.%@@ We use a transient-grating (TG) process in a Kerr bulk medium to clean a femtosecond laser pulse.Using the technique, the temporal contrast of the generated TG signal is improved by more than two orders of magnitude in comparison with the incident pulse in a 0.5-mm-thick fused silica plate.The laser spectrum is smoothed and broadened, and the pulse duration is shortened simultaneously.We expect to extend this technique to a clean pulse with broadband spectral bandwidth at a wide spectral range because it is a phase-matched process.

  4. DEMONSTRATION OF A LIQUID CARBON DIOXIDE PROCESS FOR CLEANING METAL PARTS

    Science.gov (United States)

    The report gives results of a demonstration of liquid carbon dioxide (LCO2) as an alternative to chlorinated solvents for cleaning metal parts. It describes the LCO2 process, the parts tested, the contaminants removed, and results from preliminary laboratory testing and on-site d...

  5. NATO/CCMS PILOT STUDY - CLEAN PRODUCTS AND PROCESSES (PHASE I) 2000 ANNUAL REPORT, NUMBER 242

    Science.gov (United States)

    This annual report presents the proceedings of the Third Annual NATO/CCMS pilot study meeting in Copenhagen, Denmark. Guest speakers focused on efforts in the area of research of clean products and processes, life cycle analysis, computer tools and pollution prevention.

  6. NATO CCMS PILOT STUDY ON CLEAN PRODUCTS AND PROCESSES -(PHASE I) - 2002 ANNUAL REPORT

    Science.gov (United States)

    The annual report summarizes the activities of the NATO CCMS Pilot Study on clean products and processes for 2002, including the proceedings of the 2002 annual meeting held in Vilnius, Lithuania. The report presents a wealth of information on cleaner production activities in ove...

  7. NATO/CCMS PILOT STUDY CLEAN PRODUCTS AND PROCESSES (PHASE II) 2003 ANNUAL REPORT

    Science.gov (United States)

    The 6th annual meeting of the NATO CCMS Pilot Study, Clean Products and Processes, was held in Cetraro, Italy, from May 11 to 15, 2003. This was also the first meeting of its Phase II study. 24 country representatives attended this meeting. This meeting was very ably run by th...

  8. Petroleum coke and plants : impact on growth and physiology

    International Nuclear Information System (INIS)

    Petroleum coke, a by-product of the oil sand processing industry in Alberta, contains fairly significant concentrations of arsenic, boron, iron, nickel, sulphur, titanium, and vanadium embedded in a carbon matrix. Through weathering and biological degradation, these components may be released from coke and absorbed by plant tissues where they may restrict growth and interfere with physiological activities. In order to study the effects of petroleum coke on plants, several greenhouse experiments were conducted by growing Agropyron trachycaulum, Deschampsia caespitosa, Calamagrostis canadensis, Oryzopsis hymenoides, Triticum aestivum, Cornus sericea and Fragaria virginiana for 3 months in control soil, Syncrude Canada Ltd. coke; and Suncor Energy Inc.coke. It was found that in all coke treated plants, shoot biomass was lower than controls. Root biomass followed this same trend, with the exception of Triticum aestivum. Several results were presented in this study abstract. It was concluded that the short term effects of coke on plants are most likely due to water stress and nutrient deficiency and that further research is needed

  9. A Medium-Scale 50 MW fuel Biomass Gasification Based Bio-SNG Plant: A Developed Gas Cleaning Process

    OpenAIRE

    Ramiar Sadegh-Vaziri; Marko Amovic; Rolf Ljunggren; Klas Engvall

    2015-01-01

    Natural gas is becoming increasingly important as a primary energy source. A suitable replacement for fossil natural gas is bio-SNG, produced by biomass gasification, followed by methanation. A major challenge is efficient gas cleaning processes for removal of sulfur compounds and other impurities. The present study focuses on development of a gas cleaning step for a product gas produced in a 50 MW fuel gasification system. The developed gas cleaning washing process is basically a modificatio...

  10. A Medium-Scale 50 MWfuel Biomass Gasification Based Bio-SNG Plant: A Developed Gas Cleaning Process

    OpenAIRE

    Ramiar Sadegh-Vaziri; Marko Amovic; Rolf Ljunggren; Klas Engvall

    2015-01-01

    Natural gas is becoming increasingly important as a primary energy source. A suitable replacement for fossil natural gas is bio-SNG, produced by biomass gasification, followed by methanation. A major challenge is efficient gas cleaning processes for removal of sulfur compounds and other impurities. The present study focuses on development of a gas cleaning step for a product gas produced in a 50 MWfuel gasification system. The developed gas cleaning washing process is basically a modificatio...

  11. EXPLORING ENGINEERING CONTROL THROUGH PROCESS MANIPULATION OF RADIOACTIVE LIQUID WASTE TANK CHEMICAL CLEANING

    Energy Technology Data Exchange (ETDEWEB)

    Brown, A.

    2014-04-27

    One method of remediating legacy liquid radioactive waste produced during the cold war, is aggressive in-tank chemical cleaning. Chemical cleaning has successfully reduced the curie content of residual waste heels in large underground storage tanks; however this process generates significant chemical hazards. Mercury is often the bounding hazard due to its extensive use in the separations process that produced the waste. This paper explores how variations in controllable process factors, tank level and temperature, may be manipulated to reduce the hazard potential related to mercury vapor generation. When compared using a multivariate regression analysis, findings indicated that there was a significant relationship between both tank level (p value of 1.65x10{sup -23}) and temperature (p value of 6.39x10{sup -6}) to the mercury vapor concentration in the tank ventilation system. Tank temperature showed the most promise as a controllable parameter for future tank cleaning endeavors. Despite statistically significant relationships, there may not be confidence in the ability to control accident scenarios to below mercury’s IDLH or PAC-III levels for future cleaning initiatives.

  12. The effect of wash cleaning and demagnetization process on the fly ash physico-chemical properties

    Directory of Open Access Journals (Sweden)

    A. Baliński

    2007-04-01

    Full Text Available Problems related in this study concern the possibility of improving the physico-chemical properties of fly ash used as a base granular material in moulding mixtures. The investigations were carried out mainly to evaluate the process of the fly ash modification performed in order to stabilize its mineralogical and chemical composition. Changes in chemical composition, specific surface and helium density of fly ash after the process of its wash cleaning and demagnetization were examined. The analysis of the data has proved that the process of wash cleaning considerably reduces the content of sodium and potassium. Calcium and magnesium are washed out, too. The wash cleaning process of fly ash reduces also its true density. This fact can be due to the washing out of illite as well as some fractions of haematite (the grains weakly bonded to the glassy phase. The process of demagnetization allows removing about 25.7% of the magnetic phase calculated in terms of Fe2O3. The process of demagnetization is accompanied by a decrease in the content of aluminium, sodium, potassium and calcium, and a reduction in the size of the specific surface by over one half. The possible processes of transformation have also been discussed.

  13. Steam Generator Chemical Cleaning, EPRI/SGOG Process at Asco 1 and 2 NPP

    International Nuclear Information System (INIS)

    In 2014, Westinghouse applied the EPRI/SGOG chemical cleaning process to remove hard deposits the top of the tube/sheet of the Steam Generators (SG) at the Asco Nuclear Plant Unit 1 and Unit 2. the project was very successful in meeting its goal of removing a large amount of deposits from the SGs while minimizing corrosion of the steam generator materials of construction. The process was successfully implemented with no personnel injuries and no safety or environmental events. (Author)

  14. Modeling elementary reactions in coke formation from first principles

    OpenAIRE

    Van Speybroeck, Veronique; Hemelsoet, Karen; Minner, Bert; Guy B. Marin; WAROQUIER, MICHEL

    2009-01-01

    Abstract Theoretical calculations are presented on elementary reactions which are important during coke formation in a thermal cracking unit. This process is known to proceed through a free radical chain mechanism. The elementary reaction steps that lead to the growth of the coke surface can be divided into five classes of reversible reactions : hydrogen abstraction, substitution, gas phase olefin addition to radical surface species, gas phase radical addition to ...

  15. Automatic combustion control of the ArcelorMittal Tubarao coke oven batteries

    Energy Technology Data Exchange (ETDEWEB)

    L. Barbosa de Oliveira Mello; C.-H. Sampaio Dandrea; G.-H. Marietto Goncalves; A. Estevao Torres; N.-L. Biccas

    2008-05-15

    The objective of the automatic combustion control is to guarantee the operational stability of the coke batteries based on the control of the coking time and consequently, minimize the reduction of useful life of the ovens. This control is guided by a mathematical model whose inputs are process variables and raw materials parameters and outputs are combustion parameters. Therefore, this paper will present the evolution of the performance of the burning process, providing a stability of the coking time.

  16. Preparation and characterization of bi-metallic nanoparticle catalyst having better anti-coking properties using reverse micelle technique

    Science.gov (United States)

    Zacharia, Thomas

    Energy needs are rising on an exponential basis. The mammoth energy sources like coal, natural gas and petroleum are the cause of pollution. The large outcry for an alternate energy source which is environmentally friendly and energy efficient is heard during the past few years. This is where “Clean-Fuel” like hydrogen gained its ground. Hydrogen is mainly produced by steam methane reforming (SMR). An alternate sustainable process which can reduce the cost as well as eliminate the waste products is Tri-reforming. In both these reforming processes nickel is used as catalyst. However as the process goes on the catalyst gets deactivated due to coking on the catalytic surface. This goal of this thesis work was to develop a bi-metallic catalyst which has better anti-coking properties compared to the conventional nickel catalyst. Tin was used to dope nickel. It was found that Ni3Sn complex around a core of Ni is coking resistant compared to pure nickel catalyst. Reverse micelle synthesis of catalyst preparation was used to control the size and shape of catalytic particles. These studies will benefit researches on hydrogen production and catalyst manufactures who work on different bi-metallic combinations.

  17. Prediction of coking dynamics for wet coal charge

    Directory of Open Access Journals (Sweden)

    Kardaś Dariusz

    2015-09-01

    Full Text Available A one-dimensional transient mathematical model describing thermal and flow phenomena during coal coking in an oven chamber was studied in the paper. It also accounts for heat conduction in the ceramic oven wall when assuming a constant temperature at the heating channel side. The model was solved numerically using partly implicit methods for gas flow and heat transfer problems. The histories of temperature, gas evolution and internal pressure were presented and analysed. The theoretical predictions of temperature change in the centre plane of the coke oven were compared with industrialscale measurements. Both, the experimental data and obtained numerical results show that moisture content determines the coking process dynamics, lagging the temperature increase above the water steam evaporation temperature and in consequence the total coking time. The phenomenon of internal pressure generation in the context of overlapping effects of simultaneously occurring coal transitions - devolatilisation and coal permeability decrease under plastic stage - was also discussed.

  18. Petroleum coke slags :characterization and dissolution

    OpenAIRE

    Lu, Jun

    1997-01-01

    Slags are crystalline to vitreous by-product materials generated in many high temperature industrial processes. This study presents a general technique for the identification of the phases present in petroleum coke gasification slags. documents the phase assemblages and textures, and finally determines the dissolution of vanadium from these slags as part of the considerations of potential resource reclamation. The general identification procedure utilizes (1) recognition of separa...

  19. Technology for Coking of Heavy Crude Oil with High Acid Number

    Institute of Scientific and Technical Information of China (English)

    Jiang Wen; Zhao Yujun; Cheng Gang; Li Chao; Shen Haiping; Cui Long

    2005-01-01

    Sudan Khartoum Refinery Co. has selected a unique route featuring delayed coking of crude in connection with the highly sour and high-calcium heavy crude extracted from Sudanese oil block No. 6.The crude oil after pretreatment for calcium removal is subjected to coking for removal of acids and metals with the coker products being further processed. The crude oil extracted from Sudanese oil block No. 6contains as high as 13 mg KOH/g of crude in addition to a calcium content of 1600 ppm. This article makes an analysis on problems related with the operation of commercial delayed coking unit for processing of highly sour crude and bring forth measures to solve these problems. The liquid yield resulted from coking of crude oil can reach 82m%, and the petroleum coke can meet the quality requirement for class 3B petroleum coke.

  20. Effects of Annealing on Microstructure and Microstrength of Metallurgical Coke

    Science.gov (United States)

    Xing, Xing; Zhang, Guangqing; Rogers, Harold; Zulli, Paul; Ostrovski, Oleg

    2013-12-01

    Two metallurgical cokes were heat treated at 1673 K to 2273 K (1400 °C to 2000 °C) in a nitrogen atmosphere. The effect of heat treatment on the microstructure and microstrength of metallurgical cokes was characterized using X-ray diffraction, Raman spectroscopy, and ultra-microindentation. In the process of heat treatment, the microstructure of the metallurgical cokes transformed toward the graphite structure. Raman spectroscopy of reactive maceral-derived component (RMDC) and inert maceral-derived component (IMDC) indicated that the graphitisation degree of the RMDC was slightly lower than that of the IMDC in the original cokes; however graphitisation of the RMDC progressed faster than that of the IMDC during annealing, and became significantly higher after annealing at 2273 K (2000 °C). The microstrength of cokes was significantly degraded in the process of heat treatment. The microstrength of the RMDC was lower, and of its deterioration caused by heat treatment was more severe than IMDC. The degradation of the microstrength of cokes was attributed to their increased graphitisation degree during the heat treatment.

  1. System for reducing emissions during coke oven charging; System zur Emissionsverringerung beim Fuellen von Koksoefen

    Energy Technology Data Exchange (ETDEWEB)

    Schuecker, Franz-Josef [ThyssenKrupp Industrial Solutions AG, Dortmund (Germany). Head of Oven Machine Dept., Coke Plant Technologies

    2014-10-01

    This article describes a process which reduces emissions from coke production in coke plants. The focus is on the charging process, which can be partly responsible for the fact that statutory emissions limits, which were originally met, are exceeded as coke plants get older. This article presents a solution in the form of a newly developed system that allows the oven charging system - the charging car - to respond to age-related changes in the geometry of a coke oven and thereby reduce the level of emissions.

  2. Cleaning and sanitation of Salmonella-contaminated peanut butter processing equipment.

    Science.gov (United States)

    Grasso, Elizabeth M; Grove, Stephen F; Halik, Lindsay A; Arritt, Fletcher; Keller, Susanne E

    2015-04-01

    Microbial contamination of peanut butter by Salmonella poses a significant health risk as Salmonella may remain viable throughout the product shelf life. Effective cleaning and sanitation of processing lines are essential for preventing cross-contamination. The objective of this study was to evaluate the efficacy of a cleaning and sanitation procedure involving hot oil and 60% isopropanol, ± quaternary ammonium compounds, to decontaminate pilot-scale processing equipment harboring Salmonella. Peanut butter inoculated with a cocktail of four Salmonella serovars (∼ 7 log CFU/g) was used to contaminate the equipment (∼ 75 L). The system was then emptied of peanut butter and treated with hot oil (90 °C) for 2 h followed by sanitizer for 1 h. Microbial analysis of food-contact surfaces (7 locations), peanut butter, and oil were conducted. Oil contained ∼ 3.2 log CFU/mL on both trypticase soy agar with yeast extract (TSAYE) and xylose lysine deoxycholate (XLD), indicating hot oil alone was not sufficient to inactivate Salmonella. Environmental sampling found 0.25-1.12 log CFU/cm(2) remaining on processing equipment. After the isopropanol sanitation (± quaternary ammonium compounds), no Salmonella was detected in environmental samples on XLD (<0.16 log CFU/cm(2)). These data suggest that a two-step hot oil clean and isopropanol sanitization treatment may eliminate pathogenic Salmonella from contaminated equipment. PMID:25475272

  3. Extensive separations (CLEAN) processing strategy compared to TRUEX strategy and sludge wash ion exchange

    International Nuclear Information System (INIS)

    Numerous pretreatment flowsheets have been proposed for processing the radioactive wastes in Hanford's 177 underground storage tanks. The CLEAN Option is examined along with two other flowsheet alternatives to quantify the trade-off of greater capital equipment and operating costs for aggressive separations with the reduced waste disposal costs and decreased environmental/health risks. The effect on the volume of HLW glass product and radiotoxicity of the LLW glass or grout product is predicted with current assumptions about waste characteristics and separations processes using a mass balance model. The prediction is made on three principal processing options: washing of tank wastes with removal of cesium and technetium from the supernatant, with washed solids routed directly to the glass (referred to as the Sludge Wash C processing strategy); the previous steps plus dissolution of the solids and removal of transuranic (TRU) elements, uranium, and strontium using solvent extraction processes (referred to as the Transuranic Extraction Option C (TRUEX-C) processing strategy); and an aggressive yet feasible processing strategy for separating the waste components to meet several main goals or objectives (referred to as the CLEAN Option processing strategy), such as the LLW is required to meet the US Nuclear Regulatory Commission Class A limits; concentrations of technetium, iodine, and uranium are reduced as low as reasonably achievable; and HLW will be contained within 1,000 borosilicate glass canisters that meet current Hanford Waste Vitrification Plant glass specifications

  4. Extensive separations (CLEAN) processing strategy compared to TRUEX strategy and sludge wash ion exchange

    Energy Technology Data Exchange (ETDEWEB)

    Knutson, B.J.; Jansen, G.; Zimmerman, B.D.; Seeman, S.E. [Westinghouse Hanford Co., Richland, WA (United States); Lauerhass, L.; Hoza, M. [Pacific Northwest Lab., Richland, WA (United States)

    1994-08-01

    Numerous pretreatment flowsheets have been proposed for processing the radioactive wastes in Hanford`s 177 underground storage tanks. The CLEAN Option is examined along with two other flowsheet alternatives to quantify the trade-off of greater capital equipment and operating costs for aggressive separations with the reduced waste disposal costs and decreased environmental/health risks. The effect on the volume of HLW glass product and radiotoxicity of the LLW glass or grout product is predicted with current assumptions about waste characteristics and separations processes using a mass balance model. The prediction is made on three principal processing options: washing of tank wastes with removal of cesium and technetium from the supernatant, with washed solids routed directly to the glass (referred to as the Sludge Wash C processing strategy); the previous steps plus dissolution of the solids and removal of transuranic (TRU) elements, uranium, and strontium using solvent extraction processes (referred to as the Transuranic Extraction Option C (TRUEX-C) processing strategy); and an aggressive yet feasible processing strategy for separating the waste components to meet several main goals or objectives (referred to as the CLEAN Option processing strategy), such as the LLW is required to meet the US Nuclear Regulatory Commission Class A limits; concentrations of technetium, iodine, and uranium are reduced as low as reasonably achievable; and HLW will be contained within 1,000 borosilicate glass canisters that meet current Hanford Waste Vitrification Plant glass specifications.

  5. NATO/CCMS PILOT STUDY CLEAN PRODUCTS AND PROCESSES (PHASE 1) 1998 ANNUAL REPORT (EPA/600/R-98/065)

    Science.gov (United States)

    This annual report presents the proceedings of the first annual NATO/CCMS pilot study meeting in Cincinnati in March 1998. Guest speakers focused on efforts in the research arena of clean products, clean processes, life cycle analysis, ecolabeling, and pollution prevention tools.

  6. Transformations of pyrite during formation of metallurgical coke

    Energy Technology Data Exchange (ETDEWEB)

    Stanislav Gornostayev; Jouko Haerkki; Olavi Kerkkonen [University of Oulu, Oulu (Finland). Laboratory of Process Metallurgy

    2009-10-15

    The desulfurization of pyrite during the coking process leads to the formation of phases of varying size, shape and composition. The phases are represented mostly by Fe and S-bearing associations, which can be divided into two categories: those represented only by of Fe-S phases (three varieties), and aggregates containing both sulfides and almost pure iron. There are also Fe-O and Fe-S-O phases, which were probably formed after the coke was pushed from the coke oven. It is suggested that the formation of Fe and S-bearing associations can cause the appearance of cracks and cavities in the coke matrix, which, together with the pressure of the released SO{sub 2} gas, will detract from the strength of the coke. Large grains of pyrite can create weaker spots than do smaller ones, and the incomplete decomposition of pyrite will cause migration of the remaining part of the sulfur to the blast furnace, affecting the reactions there. This may be more common in cokes of relatively low porosity and small pore size and in those made from coals with large pyrite grains. 17 refs., 2 figs., 1 tab.

  7. Experimental study on the advanced treatment of bio-chemically treated coking wastewater by the advanced Fenton oxidation process%Fenton高级氧化法深度处理焦化生化废水的实验研究

    Institute of Scientific and Technical Information of China (English)

    杨水莲; 田晓媛; 吴滨; 王威燕; 杨运泉

    2014-01-01

    The Fenton reagent used was made from ferrous sulphate and hydrogen peroxide. It is used in the advanced treatment of coking wastewater which was bio-chemically treated. The effects of the initial pH ,and dosages of FeSO4·7H2O,H2O2 and PAM on the treatment effectiveness of the bio-chemically treated coking wastewater have been investigated. The results show that using the advanced Fenton oxidation process can effectively remove the COD,NH3-N and chroma from this kind of coking wastewater. For bio-chemically treated coking wastewater with moderate concentration,the optimum conditions for Fenton oxidation process are as follows:the initial pH of waste-water is 8-10,dosage of FeSO4·7H2O 500 mg/L,dosage of H2O2 3.5 mL/L,and dosage of PAM 4.0 mg/L. Under these conditions,the removing rates of COD,NH3-N and Chroma can reach 85.9%,97.3%and 84.6%,respectively.%采用硫酸亚铁和过氧化氢所构成的Fenton试剂,对经生化处理后的焦化废水进行Fenton高级氧化深度处理,重点考察了废水初始pH,FeSO4·7H2O、H2O2及PAM投加量对焦化生化废水处理效果的影响。结果表明,采用Fenton高级氧化法可使经生化处理后的焦化废水中的COD、NH3-N和色度得到进一步有效去除。对于中等浓度的焦化生化废水,较适宜的Fenton氧化工艺条件:废水初始pH为8~10,FeSO4·7H2O投加量为500 mg/L,H2O2投加量为3.5 mL/L,PAM投加量为4.0 mg/L。在此条件下, COD、NH3-N和色度的去除率分别可达85.9%、97.3%和84.6%。

  8. The History and Future Challenges of Calcined Petroleum Coke Production and Use in Aluminum Smelting

    Science.gov (United States)

    Edwards, Les

    2015-02-01

    Calcined petroleum coke is used for the production of carbon anodes in the Hall-Héroult aluminum smelting process due to a combination of low impurity levels, ready availability, and relatively low cost. This article provides a review of the history and use of calcined petroleum coke for anode production and describes the different calcining technologies used by the industry. The article discusses the impact of changes in crude oil quality and refining economics over the last 10 years as well as the impact on green petroleum coke quality and availability. The industry has adapted well to quality changes in recent times, and the blending of different quality cokes by smelters is becoming increasingly important. The world has a plentiful supply of green petroleum coke, but the next wave of aluminum smelting capacity growth will put further pressure on the supply of the higher quality cokes traditionally favored by the industry.

  9. Automated cleaning and pre-processing of immunoglobulin gene sequences from high-throughput sequencing

    Directory of Open Access Journals (Sweden)

    Miri eMichaeli

    2012-12-01

    Full Text Available High throughput sequencing (HTS yields tens of thousands to millions of sequences that require a large amount of pre-processing work to clean various artifacts. Such cleaning cannot be performed manually. Existing programs are not suitable for immunoglobulin (Ig genes, which are variable and often highly mutated. This paper describes Ig-HTS-Cleaner (Ig High Throughput Sequencing Cleaner, a program containing a simple cleaning procedure that successfully deals with pre-processing of Ig sequences derived from HTS, and Ig-Indel-Identifier (Ig Insertion – Deletion Identifier, a program for identifying legitimate and artifact insertions and/or deletions (indels. Our programs were designed for analyzing Ig gene sequences obtained by 454 sequencing, but they are applicable to all types of sequences and sequencing platforms. Ig-HTS-Cleaner and Ig-Indel-Identifier have been implemented in Java and saved as executable JAR files, supported on Linux and MS Windows. No special requirements are needed in order to run the programs, except for correctly constructing the input files as explained in the text. The programs' performance has been tested and validated on real and simulated data sets.

  10. Benefits of integrating chemical and mechanical cleaning processes for steam generator sludge removal

    International Nuclear Information System (INIS)

    This paper discusses the benefits of performing in-bundle tubesheet lancing in conjunction with chemical cleaning of PWR and PHWR steam generators in which a hard sludge pile is known to exist. The primary benefits of in-bundle lancing are to: (1) increase the exposed area of the sludge pile by cutting furrows in the surface thereby enhancing dissolution of sludge, (2) reduce the volume of solvents required since material removed by lancing does not have to be dissolved chemically, (3) improve rinsing and removal of residual solvent between iron and copper dissolution steps, and (4) allow for verification of process effectiveness by providing high quality in-bundle visual inspection. The reduction in solvent volumes can lead to a significant reduction in solvent costs and waste processing. A case study which includes an economic evaluation for a combined chemical and mechanical cleaning shows a potential cost saving of up to US$ 300,000 over use of chemical cleaning alone. 14 refs., 2 tabs., 2 figs

  11. Silica Brick for Coke Oven

    Institute of Scientific and Technical Information of China (English)

    Wang Jing

    2007-01-01

    @@ 1 Scope This standard specifies the classification,specification,test method,quality appraisal procedure,labeling,packing,transportation,storage and quality certification of silica brick for coke oven.

  12. PROSPECTS FOR COKE BREEZE RECOVERY

    Directory of Open Access Journals (Sweden)

    D. N. Mihnovets

    2012-01-01

    Full Text Available Researches give grounds to believe in the possibility of receiving briquettes from coke waste mixed with peat dry coal and their use for smelting iron in the cupola or as a household fuel.

  13. Application of non-invasive optical monitoring methodologies to follow and record painting cleaning processes

    Science.gov (United States)

    Fontana, R.; Dal Fovo, A.; Striova, J.; Pezzati, L.; Pampaloni, E.; Raffaelli, M.; Barucci, M.

    2015-11-01

    The cleaning of painted artworks, i.e. the critical operation whereby materials are selectively removed from a painted surface by partial thinning or complete elimination of varnish, is one of the most debated conservation operations, being an irreversible process, which may result in chromatic and morphological variations in the painted surface. Due to ageing, the upper layer is subject to darkening and yellowing because of blanching and fading from ultraviolet exposure, dust deposition, and overpainted layers due, for instance, to restoration interventions. This degradation can either alter the original appearance of painting polychromy or cause mechanical failure of the finishes. To address these adverse conditions, a process of examination and analysis is critical to the definition and interpretation of the varnish layer. When investigating the ageing process of old paintings, it is of great importance to obtain insight into the painting technique as practiced in the past, and the first step in gaining this knowledge is, to a large extent, based on the study of the varnish film. An effective control of the process and objective evaluation of its outcome requires therefore instrumental/analytical support. The present study illustrates the successful application of non-invasive optical techniques—such as colorimetry, multispectral reflectography, laser scanning micro-profilometry, and optical coherence tomography—to the monitoring of an Italian fourteenth-century painting cleaning process. Results presented here confirm that optical techniques play a pivotal role in artwork diagnostics, especially with regard to conservation operations, while also indicating their validity when applied to the monitoring of the cleaning process.

  14. MEROS: an improved dry-type gas-cleaning process for the treatment of sinter offgas

    International Nuclear Information System (INIS)

    VAI has developed the MEROS process (Maximized Emission Reduction Of Sintering) in which dust and harmful metallic and organic components present in sinter offgas are removed in a series of treatment steps to levels previously un-attained with conventional gas-treatment techniques. In a number of test campaigns, the technical and economical advantages of this innovative sinter offgas-cleaning process were verified. Voestalpine Stahl subsequently placed an order with VAI for the installation of an industrial MEROS facility to be started-up in August 2007. (author)

  15. Fouling of a spiral-wound reverse osmosis membrane processing swine wastewater: effect of cleaning procedure on fouling resistance.

    Science.gov (United States)

    Camilleri-Rumbau, M S; Masse, L; Dubreuil, J; Mondor, M; Christensen, K V; Norddahl, B

    2016-07-01

    Swine manure is a valuable source of nitrogen, phosphorus and potassium. After solid-liquid separation, the resulting swine wastewater can be concentrated by reverse osmosis (RO) to produce a nitrogen-potassium rich fertilizer. However, swine wastewater has a high fouling potential and an efficient cleaning strategy is required. In this study, a semi-commercial farm scale RO spiral-wound membrane unit was fouled while processing larger volumes of swine wastewater during realistic cyclic operations over a 9-week period. Membrane cleaning was performed daily. Three different cleaning solutions, containing SDS, SDS+EDTA and NaOH were compared. About 99% of the fouling resistance could be removed by rinsing the membrane with water. Flux recoveries (FRs) above 98% were achieved for all the three cleaning solutions after cleaning. No significant differences in FR were found between the cleaning solutions. The NaOH solution thus is a good economical option for cleaning RO spiral-wound membranes fouled with swine wastewater. Soaking the membrane for 3 days in permeate water at the end of each week further improved the FR. Furthermore, a fouling resistance model for predicting the fouling rate, permeate flux decay and cleaning cycle periods based on processing time and swine wastewater conductivity was developed. PMID:26698296

  16. Self Cleaning High Efficiency Particulate Air (HEPA) Filtration without Interrupting Process Flow - 59347

    International Nuclear Information System (INIS)

    The strategy of protecting the traditional glass fibre HEPA filtration train from it's blinding contamination and the recovery of dust by the means of self cleaning, pre-filtration is a proven means in the reduction of ultimate disposal volumes and has been used within the Fuel Production Industry. However, there is an increasing demand in nuclear applications requiring elevated operating temperatures, fire resistance, moisture resistance and chemical composition that the existing glass fibre HEPA filtration cannot accommodate, which can be remedied by the use of a metallic HEPA filter media. Previous research suggests that the then costs to the Department of Energy (DOE), based on a five year life cycle, was $29.5 million for the installation, testing, removal and disposal of glass fibre HEPA filtration trains. Within these costs, $300 was the value given to the filter and $4, 450 was given to the peripheral activity. Development of a low cost, cleanable, metallic, direct replacement of the traditional filter train will the clear solution. The Bergman et al work has suggested that a 1000 ft3/min, cleanable, stainless HEPA could be commercially available for $5, 000 each, whereas the industry has determined that the truer cost of such an item in isolation would be closer to $15, 000. This results in a conflict within the requirement between 'low cost' and 'stainless HEPA'. By proposing a system that combines metallic HEPA filtration with the ability to self clean without interrupting the process flow, the need for a tradition HEPA filtration train will be eliminated and this dramatically reduces the resources required for cleaning or disposal, thus presenting a route to reducing ultimate costs. The paper will examine the performance characteristics, filtration efficiency, flow verses differential pressure and cleanability of a self cleaning HEPA grade sintered metal filter element, together with data to prove the contention. (authors)

  17. Processes of elimination of activated corrosion products. Chemical decontamination - fuel cleaning

    International Nuclear Information System (INIS)

    The abatement of the individual and collective dose of a PWR imposes to control the source term through different processes implemented during the plant exploitation. When the limits of these different optimization processes are reached, the abatement of dose rates requires the implementation of curative processes. The objective is thus to eliminate the contaminated oxides and deposits present on surfaces free of radiation flux, and eventually on surfaces under radiation flux and on the fuel itself. The chemical decontamination of equipments and systems is the main and universal remedy implemented at different levels. On the other hand, the ultrasonic cleaning of fuel assemblies is a promising process. This paper aims at illustrating these different techniques using concrete examples of application in France and abroad (decontamination during steam generator replacement, decontamination of primary pump scroll in hot workshop, decontamination of loop sections, ultrasonic cleaning of fuel). The description of these different operations stresses on their efficiency in terms of dosimetric gain, duration of implementation, generation of wastes, and recontamination following their implementation. (J.S.)

  18. Optimization of clean fractionation processing as a pre-treatment technology for prairie cordgrass.

    Science.gov (United States)

    Brudecki, Grzegorz; Cybulska, Iwona; Rosentrater, Kurt; Julson, James

    2012-03-01

    The main objective of this study was to fractionate prairie cordgrass (PCG) obtaining the highest cellulose digestibility. Following clean fractionation (CF) processing, the PCG lignocellulosic biomass was fractionated into three main building blocks: cellulose, hemicellulose and lignin. Effects of processing factors such as time, temperature, catalyst concentration and organic solvent mixture composition were evaluated. Organic solvent-aqueous mixture contained methyl isobutyl ketone (MIBK), ethanol and water in different proportions. Sulfuric acid was used as a catalyst. In order to evaluate the degree of pre-treatment, enzymatic saccharification was employed on the cellulose fraction obtained from the CF process. Response surface methodology was used for process optimization and statistical analysis. Optimal conditions (39 min, 154°C, 0.69% catalyst and 9% MIBK) resulted in 84% glucose yield and 87% acid insoluble lignin (AIL). PMID:22244901

  19. Relevance of the composition of municipal plastic wastes for metallurgical coke production

    Energy Technology Data Exchange (ETDEWEB)

    S. Melendi; M.A. Diez; R. Alvarez; C. Barriocanal [Instituto Nacional del Carbon (INCAR), Oviedo (Spain)

    2011-04-15

    This study is concerned with the effects of the composition of mixed plastic wastes on the thermoplastic properties of coal, the generation of coking pressure and the quality of the resulting cokes in a movable wall oven at semipilot scale. The mixed plastic wastes were selected to cover a wide spectrum in the relative proportions of high- and low-density polyethylenes (HDPE and LDPE), polypropylene (PP), polystyrene (PS) and polyethylene terephthalate (PET). From the results it was deduced that the reduction in Gieseler fluidity in the coal blend is linked to the total amount of polyolefins in the waste. It was also found that these thermoplastics increase the pressure exerted against the wall in the course of the coking process and that coke quality is maintained or even improved. However, when the level of aromatic polymers such PS and PET are increased at the expense of polyolefins, the coking pressure decreases. Thus, the amount of aromatic polymers such as PS and PET in the waste is critical, not only for controlling Gieseler fluidity and coking pressure, but also for avoiding deterioration in coke quality (reactivity towards CO{sub 2} CRI and mechanical strength of the partially-gasified coke CSR). An amount of polyolefins in the waste lower than 65 wt.% for a secure coking pressure is established. 43 refs., 7 figs., 4 tabs.

  20. Assessment of metal releases and leachate toxicity of oil sands coke

    International Nuclear Information System (INIS)

    Large volumes of coke are produced as a by-product of thermal upgrading of oil sands bitumen in Alberta. This paper examined the feasibility of integrating this stored by-product at wetland reclamation sites. Coke leachate water toxicity was evaluated in this study since coke is known to releases trace amounts of metals when it comes in contact with water. The objective was to determine the cause of toxicity by performing toxicity identification evaluations (TIEs) on the leachate. The leachability of metals from coke was examined over a 45 day period in 2-L glass jars using reconstituted water with a hardness of 300 mg/L as calcium carbonate (CaCO3) at pH levels 5.5 and 9.5. Coke porewater samples and overlying water samples collected periodically were analyzed for trace metals using inductively coupled plasma mass spectroscopy (ICP-MS). The toxicity of coke leachate was evaluated at the end of the 45 day period using a Ceriodaphnia dubia standard three-brood chronic test with survival and reproduction as endpoints. Coke leachate water from both pH treatments had a negative effect on survival and reproduction of C. dubia. The coke leachate had high concentrations of vanadium, according to metal analysis of leachate water from both pH treatments. In order to identify the cause of toxicity, the coke leachate water will be subjected to several TIE processes

  1. Well-ordered polymer nano-fibers with self-cleaning property by disturbing crystallization process

    OpenAIRE

    Yang, Qin; Luo, Zhuangzhu; Tan, Sheng; Luo, Yimin; Wang, Yunjiao; Zhang, Zhaozhu; Liu, Weimin

    2014-01-01

    Bionic self-cleaning surfaces with well-ordered polymer nano-fibers are firstly fabricated by disturbing crystallization during one-step coating-curing process. Orderly thin (100 nm) and long (5–10 μm) polymer nano-fibers with a certain direction are fabricated by external macroscopic force (F blow) interference introduced by H2 gas flow, leading to superior superhydrophobicity with a water contact angle (WCA) of 170° and a water sliding angle (WSA) of 0-1°. In contrast, nano-wires and nano-b...

  2. Gasification characteristics of coke and mixture with coal in an entrained-flow gasifier

    Energy Technology Data Exchange (ETDEWEB)

    See Hoon Lee; Sang Jun Yoon; Ho Won Ra; Young Il Son; Jai Chang Hong; Jae Goo Lee [Korean Institute of Energy Research, Taejon (Republic of Korea). Gasification Research Group

    2010-08-15

    To enhance clean energy utilization and reduce greenhouse gases, various gasification technologies have been developed in the world. The gasification characteristics, such as syngas flow rate, compositions, cold gas efficiency and carbon conversion, of petroleum coke and mixture of petroleum coke and lignite were investigated in a 1 T/d entrained-flow gasifier (ID. 0.2 m x height 1.7 m) with quencher as a syngas cooler. CO concentration was 31-42 vol% and H{sub 2} concentration was almost 22 vol% in the gasification experiments of petroleum coke. In the case of mixture of petroleum coke and lignite, CO concentration was 37-47 vol% and H{sub 2} concentration was almost 25 vol% due to synergy effect. The gasification of mixture resulted in higher syngas heating value and cold gas efficiency because of the higher H{sub 2} and CO composition in syngas.

  3. Gasification characteristics of coke and mixture with coal in an entrained-flow gasifier

    Energy Technology Data Exchange (ETDEWEB)

    Lee, See Hoon; Yoon, Sang Jun; Ra, Ho Won; Son, Young Il; Hong, Jai Chang; Lee, Jae Goo [Gasification Research Group, Korea Institute of Energy Research, 71-2 Jang-dong, Yuseong-gu, Daejeon 305-343 (Korea)

    2010-08-15

    To enhance clean energy utilization and reduce greenhouse gases, various gasification technologies have been developed in the world. The gasification characteristics, such as syngas flow rate, compositions, cold gas efficiency and carbon conversion, of petroleum coke and mixture of petroleum coke and lignite were investigated in a 1 T/d entrained-flow gasifier (I.D. 0.2 m x height 1.7 m) with quencher as a syngas cooler. CO concentration was 31-42 vol% and H{sub 2} concentration was almost 22 vol% in the gasification experiments of petroleum coke. In the case of mixture of petroleum coke and lignite, CO concentration was 37-47 vol% and H{sub 2} concentration was almost 25 vol% due to synergy effect. The gasification of mixture resulted in higher syngas heating value and cold gas efficiency because of the higher H{sub 2} and CO composition in syngas. (author)

  4. Corrosion behaviour of the tool steel of the fuel charge machine during cleaning process

    International Nuclear Information System (INIS)

    In the framework of the experimentation activity of the PEC Reactor components, presently in course at the Casaccia Energy Research Centre (CRE Casaccia), the sodium removal process has been usually carried out by means of Butylcellosolve. Recently, in order to eliminate flammable organic solvent from the reactor building, it was decided to evaluate the possibility of using an atomized water method for the cleaning of the Fuel Charge Machine (FCM). Two important problems have been immediately identified: - lower removal process efficiency; since the geometries of the PEC Reactor FCM are complex, there are a number of areas of retention, where liquid access is difficult, - component damage due to the corrosion process. The main risk is associated with the formation of aqueous NaOH which can give rise to caustic stress corrosion cracking. In order to know something more about the above mentioned problems, a test programme was designed whose main aims were: - cleaning tests efficiency determination of gripper prototype by atomized water method using nitrogen gas or alternatively carbon dioxide; - study of the corrosion behaviour of tool steel in caustic solutions. This paper reports the results of the corrosion tests

  5. Development of an on-line process for steam generator chemical cleaning

    Energy Technology Data Exchange (ETDEWEB)

    Semmler, J.; Guzonas, D.A.; Rousseau, S.C.; Snaglewski, A.P.; Chenier, M.P. [Atomic Energy of Canada Limited, Chalk River, Ontario (Canada)

    1998-07-01

    An on-line, preventative chemical cleaning process for the removal of secondary side oxides from steam generators is being developed. An on-line chemical cleaning process uses a low concentration of a chelant ({approx}1-10 mg L{sup -1}) to partially dissolve and dislodge the secondary side oxides while the steam generator is in operation. The dissolved and dislodged oxides can then be removed by blowdown. Feasibility tests were carried out in which the operating conditions of a CANDU steam generator were simulated in an autoclave containing either loose powdered magnetite or sintered magnetite on Alloy 800 (I-800) steam generator tube surfaces. The extent of magnetite dissolution in on-line solvent formulations containing either ethylenediaminetetraacetic acid (EDTA) or N-(2-hydroxyethyl)ethylenedinitrilo-N,N',N'-triacetic acid (HEDTA) at temperatures of 256 and 263 degrees C were measured. Powdered magnetite dissolved faster than sintered magnetite using both types of chelant. Dissolution continued as fresh chelant was added. The half-life (t{sup 1/2}) of Fe-EDTA complexes at 256 degrees C was approximately 3 h, sufficient to allow removal by blowdown. Hydrazine and morpholine were equally effective as oxygen scavengers. Increased dissolved oxygen concentration was found to result in chelant decomposition, reduced solvent capacity and increased carbon steel corrosion. Total corrosion of several materials relevant to CANDU stations were measured in 96-h tests. To minimize corrosion, low concentration of chelant and a high concentration of an oxygen scavenger should be used. The results from these feasibility tests are currently being used to define the application conditions for large-scale tests of on-line chemical cleaning in a model steam generator. (author)

  6. Development of an on-line process for steam generator chemical cleaning

    International Nuclear Information System (INIS)

    An on-line, preventative chemical cleaning process for the removal of secondary side oxides from steam generators is being developed. An on-line chemical cleaning process uses a low concentration of a chelant (∼1-10 mg L-1) to partially dissolve and dislodge the secondary side oxides while the steam generator is in operation. The dissolved and dislodged oxides can then be removed by blowdown. Feasibility tests were carried out in which the operating conditions of a CANDU steam generator were simulated in an autoclave containing either loose powdered magnetite or sintered magnetite on Alloy 800 (I-800) steam generator tube surfaces. The extent of magnetite dissolution in on-line solvent formulations containing either ethylenediaminetetraacetic acid (EDTA) or N-(2-hydroxyethyl)ethylenedinitrilo-N,N',N'-triacetic acid (HEDTA) at temperatures of 256 and 263 degrees C were measured. Powdered magnetite dissolved faster than sintered magnetite using both types of chelant. Dissolution continued as fresh chelant was added. The half-life (t1/2) of Fe-EDTA complexes at 256 degrees C was approximately 3 h, sufficient to allow removal by blowdown. Hydrazine and morpholine were equally effective as oxygen scavengers. Increased dissolved oxygen concentration was found to result in chelant decomposition, reduced solvent capacity and increased carbon steel corrosion. Total corrosion of several materials relevant to CANDU stations were measured in 96-h tests. To minimize corrosion, low concentration of chelant and a high concentration of an oxygen scavenger should be used. The results from these feasibility tests are currently being used to define the application conditions for large-scale tests of on-line chemical cleaning in a model steam generator. (author)

  7. 46 CFR 148.04-15 - Petroleum coke, uncalcined; petroleum coke, uncalcined and calcined (mixture).

    Science.gov (United States)

    2010-10-01

    ... 46 Shipping 5 2010-10-01 2010-10-01 false Petroleum coke, uncalcined; petroleum coke, uncalcined and calcined (mixture). 148.04-15 Section 148.04-15 Shipping COAST GUARD, DEPARTMENT OF HOMELAND... Requirements for Certain Material § 148.04-15 Petroleum coke, uncalcined; petroleum coke, uncalcined...

  8. Procedures for Efficient and Economic Recovery of Heat for Reuse in Batch Processes for Cleaning

    DEFF Research Database (Denmark)

    Qvale, Einar Bjørn

    2005-01-01

    The expenditure of primary energy can be reduced and the economics of process plants in the food industry can be improved by intelligent application of Process Integration (PI). Since a greater part of the products in the food industry is processed in batches, the use of Thermal- Energy Storage...... (TES) may be required to achieve these improvements. Further improvements may be achieved if there is a need, in the plant, for heating water at low-or-medium-level temperatures for cleaning purposes and there are significant quantities of medium-to-lowtemperature heat recoverable. Such conditions are......, could increase the use and usefulness of PI by incorporating TES, thus fulfilling PI’s promises of improved operation, reduced energy consumption, reduced environmental impact, and improved economics. The application of these procedures is illustrated through the description of two cases. Keywords: Heat...

  9. Procedures for Efficient and Economic Recovery of Heat for Reuse in Batch Processes for Cleaning

    DEFF Research Database (Denmark)

    Qvale, Einar Bjørn

    The expenditure of primary energy can be reduced and the economics of process plants in the food industry can be improved by intelligent application of Process Integration (PI). Since a greater part of the products in the food industry is processed in batches, the use of Thermal- Energy Storage...... (TES) may be required to achieve these improvements. Further improvements may be achieved if there is a need, in the plant, for heating water at low-or-medium-level temperatures for cleaning purposes and there are significant quantities of medium-to-lowtemperature heat recoverable. Such conditions are......, could increase the use and usefulness of PI by incorporating TES, thus fulfilling PI’s promises of improved operation, reduced energy consumption, reduced environmental impact, and improved economics. The application of these procedures is illustrated through the description of two cases. Keywords: Heat...

  10. Isotopic compositions of s-process elements in acid-cleaned mainstream presolar silicon carbide

    Science.gov (United States)

    Liu, Nan

    Pristine meteorites contain ancient stellar relicts that survived destructions in the early solar system. Isotopic studies of these presolar grains have proven to be a unique method to understand various known and unknown nucleosynthetic processes occurred in their parent stars. Previous studies of isotopic compositions of heavy elements in mainstream SiC grains from low-mass asymptotic giant branch (AGB) stars reported contamination from solar system materials with normal isotopic compositions on grain surfaces and prevented the authors from obtaining the pure nucleosynthetic isotopic signature from stars. In addition, in these previous studies uncertainties in the major neutron source 13C within the 13C-pocket were underestimated because only the 13C mass fraction was considered as a parameter with the 13C-pocket mass and the 13C profile fixed in model calculations. The oversimplified treatment of the 13C-pocket mainly resulted from the fact that it was unclear if there exists any tracer to distinguish different effects of the 13C concentration, the 13C-pocket mass, and the 13C profile within the 13C-pocket. To address these issues, we acid-cleaned all the presolar SiC grains used in this study after their separation from the bulk Murchison meteorite. In addition, we chose to measure strontium and barium isotopic compositions in these acid-cleaned SiC grains, because both elements sit at the first and second s-process peaks along the s-process path, and are sensitive to varying parameters for the s-process in model calculations. By comparing our new acid-cleaned grain data with single grain data from previous studies for barium isotopes, we conclude that the acid-cleaning procedure is quite effective in removing surface barium contamination. For the first time, we find that model predictions for 138Ba/ 136Ba are sensitive to all three variables of the 13C-pocket adopted in AGB model calculations. In order to match the low 138Ba/ 136Ba values in a minor group of

  11. Study on purge gas generated in coke oven gas boilers mixing-firing process%焦炉气锅炉掺烧弛放气探讨

    Institute of Scientific and Technical Information of China (English)

    高翔

    2012-01-01

    It' s not an environmental friendly and economy way to discharged purge gas from methanol plant into the atmosphere. How to recycle methanol purge gas? The treatment of purge gas had been a general concern problem. The problem could be solved by incorpo- rating the decompression purge gas into boilers burning coke oven gas used as burning gas.%甲醇厂弛放气直接排人大气,既对环境产生污染,又无法实现经济价值。通过将弛放气减压掺入焦炉煤气中供锅炉燃烧使用的方法,可以解决弛放气的去向问题。

  12. Ultrasonically treated liquid interfaces for progress in cleaning and separation processes.

    Science.gov (United States)

    Radziuk, Darya; Möhwald, Helmuth

    2016-01-01

    Ultrasound and acoustic cavitation enable ergonomic and eco-friendly treatment of complex liquids with outstanding performance in cleaning, separation and recycling of resources. A key element of ultrasonic-based technology is the high speed of mixing by streams, flows and jets (or shock waves), which is accompanied by sonochemical reactions. Mass transfer across the phase boundary with a great variety of catalytic processes is substantially enhanced through acoustic emulsification. Encapsulation, separation and recovery of liquids are fast with high production yield if applied by ultrasound. Here we discuss the state of knowledge of these processes by ultrasound and acoustic cavitation from a perspective of a physico-chemical model in order to predict and control the outcome. We focus on the physical interpretation and quantification of ultrasonic parameters and properties of liquids to understand the chemistry of liquid/liquid interfaces in acoustic fields. The roles of thermodynamic enthalpy and entropy (incl. Laplace and osmotic pressure) in the context of sonochemical reactions (separation, catalysis, degradation, cross-linking, ion exchange and phase transfer) are outlined. The synergy of ultrasound and electric fields or continuous flow chemistry for cleaning and separation via emulsification is highlighted by specific strategies involving polymers and ultrasonic membranes. PMID:26435267

  13. Comparison of coke burning on catalysts coked in a commericial plant and in the laboratory

    Energy Technology Data Exchange (ETDEWEB)

    Pieck, C.L.; Parera, J.M. (Instituto de Investigaciones en Catalisis y Petroquimica, Santiago del Estero 2654, 3000 Santa Fe (AR))

    1989-12-01

    This paper reports a commercial catalyst coked in a commercial naphtha reforming unit compared with a laboratory catalyst and the fresh commercial one coked during laboratory experiments at pressures lower than the commercial one. The carbon concentration on the catalyst and hydrogen/carbon ratio of the coke were measured. Temperature-programmed oxidation and test reactions for metallic and acidic functions of the coked catalysts were performed. The main difference is in the coke composition and its distribution over the catalytic functions of the catalyst. Compared to the commercially coked catalyst, the coke on the laboratory coked catalysts is richer in hydrogen, covers the metallic function in a higher proportion, and is burnt faster. The catalytic activity for hydrogenation (metallic reaction) of the laboratory-coked catalyst is decreased more, but it is partially recovered by increasing the hydrogen pressure. The decrease on the acidic activity produced by coking is similar on both catalysts.

  14. Functionalization of Petroleum Coke-Derived Carbon for Synergistically Enhanced Capacitive Performance.

    Science.gov (United States)

    Zhang, Yan; Li, Xuejin; Huang, Jufeng; Xing, Wei; Yan, Zifeng

    2016-12-01

    Petroleum coke is a valuable and potential source for clean energy storage if it could be modified legitimately and facilely. In the present study, porous carbon with high surface area and abundant oxygen-containing groups was prepared from petroleum coke by chemical activation and modification processes. The as-prepared carbon exhibits a high surface area (1129 m(2) · g(-1)) and stable micrographic structure. It presents a high specific capacitance and excellent rate performance in KOH electrolyte. Even at an ultrahigh current density of 50 A · g(-1), the specific capacitance of the prepared carbon can still reach up to an unprecedented value of 261 F · g(-1) with a superhigh retention rate of 81 %. In addition, the energy density of this material in aqueous electrolyte can be as high as 13.9 Wh · kg(-1). The high energy density and excellent rate performance ensure its prosperous application in high-power energy storage system. PMID:27009530

  15. Minimization of water and chemical usage in the cleaning in place process of a milk pasteurization plant

    Directory of Open Access Journals (Sweden)

    Sathit Niamsuwan

    2011-08-01

    Full Text Available Cleaning in place (CIP is a method of cleaning inner surfaces of piping, vessel, equipment, and associated fitting withdisassembly. Although, the CIP processes have been studied continually to improve efficiency for chemical and water consumption,the real conventional plant operations of this process still have been considered as a large amount of consumption.The objectives of this work are to study process behaviors and to find out the optimal draining ratio of the CIP cleaningchemicals in a pasteurized milk plant. To achieve these, mathematical models of the CIP process have been developed andvalidated by the actual process data. With these models, simulation study has been carried out to describe the dynamicbehaviors of the process with respect to the concentrations and contaminations in CIP cleaning chemicals. The optimizationproblem has been formulated and solved using written programs based on MATLAB application program.

  16. Clean coal technology: commercial-scale demonstration of the liquid phase methanol (LPMEOH{trademark}) process

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1999-04-01

    The report discusses the demonstration of Air Products and Chemical, Inc.`s Liquid Phase Methanol (LPMEOTH {trademark}) Process which is designed to convert synthesis gas derived from the gasification of coal into methanol for use as a chemical intermediate or as a low-sulfur dioxide and low-nitrogen oxides emitting alternative fuel. The project was selected for funding by the US Clean Coal Technology Program Round III in 1992. Construction of the Demonstration Project at Eastman Chemical Co`s Kingsport complex began in October 1995 and was completed in January 1997. Production rates of over 300 tons per day of methanol have been achieved and availability for the unit has exceeded 96% since startup. The LPMEOH{trademark} Process can enhance integrated gasification combined cycle (IGCC) power generation by converting part of the syngas from the gasifier to methanol which can be solid or used as a peak-sharing fuel. 50 refs., 5 figs., 7 photos.

  17. Intercalation mechanisms of lithium into graphitized needle cokes

    Institute of Scientific and Technical Information of China (English)

    苏玉长; 尹志民; 徐仲榆

    2001-01-01

    A needle coke was graphitized at different heat treatment temperature (2000℃ to 3000℃). The electrochemical intercalation mechanism of Li into the graphitized coke has been studied in Li|1mol*L-1 LiClO4+ethylene carbonate/diethylene carbonate|graphite cells, using an in-situ X-Ray diffraction (XRD) technique. The study of Li-C intercalation processes of the graphitized coke reveals that there are three major types of intercalation behavior. The first is uniformly intercalated at all Li-C compounds in graphitized coke heated at 2250℃; the second is obviously staging phenomenon during intercalating for the graphitized coke heated at 2750℃; the third is cointercalation of solvated Li-ion at high potential (>0.3V) and then lithium electrochemical intercalation at lower potential for that heated at 3000℃, resulting in the decrease of capacity and efficiency of graphite negative electrode for lithium-ion secondary battery.

  18. Effects of Coke Calcination Level on Pore Structure in Carbon Anodes

    Science.gov (United States)

    Fang, Ning; Xue, Jilai; Lang, Guanghui; Bao, Chongai; Gao, Shoulei

    2016-02-01

    Effects of coke calcination levels on pore structure of carbon anodes have been investigated. Bench anodes were prepared by 3 types of cokes with 4 calcination temperatures (800°C, 900°C, 1000°C and 1100°C). The cokes and anodes were characterized using hydrostatic method, air permeability determination, mercury porosimetry, image analysis and confocal microscopy (CSLM). The cokes with different calcination levels are almost the same in LC values (19-20 Å) and real density (1.967-1.985 g/cm3), while the anode containing coke calcined at 900°C has the lowest open porosity and air permeability. Pore size distribution (represented by Anode H sample) can be roughly divided into two ranges: small and medium pores in diameter of 10-400 μm and large pores of 400-580 μm. For the anode containing coke calcined at 800°C, a number of long, narrow pores in the pore size range of 400-580 μm are presented among cokes particles. Formation of these elongated pores may be attributed to coke shrinkages during the anode baking process, which may develop cracking in the anode under cell operations. More small or medium rounded pores with pore size range of 10-400 μm emerge in the anodes with coke calcination temperatures of 900°C, 1000°C and 1100°C, which may be generated due to release of volatiles from the carbon anode during baking. For the anode containing coke calcined at 1100°C, it is found that many rounded pores often closely surround large coke particles, which have potential to form elongated, narrow pores.

  19. Wear resistance of coke-crushing hammers

    OpenAIRE

    Zupanič, Franc

    2015-01-01

    This work investigated several methods for improving the wear resistance of the 42CrMo4 tool steel used for coke-crushing hammers. The methods embraced heat treatment for obtaining different combinations of strength and ductility of the bulk steel, and surface-engineering processes comprising TiN thin-film deposition using magnetron-sputtering, nitriding and WC/Ni weld deposit surfaced by gas metal arc (GMA) method. The wear-resistance was tested under industrial conditions. Oil quenching and...

  20. Economic Aspects of Air and Gas Cleaning for Nuclear Energy Processes

    International Nuclear Information System (INIS)

    In this paper the basic requirements for control of gaseous and particulate effluents are given as applied to problems of feed material production, isotope separation, fuel element fabrication, fuel recovery and reactor operation. There are also instances where non-radioactive nuclear materials with toxic or nuisance effluents such as from beryllium and zirconium production are of concern and these too must be controlled at reasonable costs. The factors involved in capital and operating costs of gas cleaning equipment and the types of applications in the United States are described in some detail. Gaseous effluent problems have, of course, been attacked and controlled by several types of device but their performance has been measured on a comparable basis. It is thus possible to judge operating characteristics on an economic basis as related to power consumption, adsorbent costs, space charges, corrosion problems and other operational factors. The United States Atomic Energy Commission through its contract with the Harvard University Air Cleaning Laboratory has initiated an evaluation program with cooperation, from the various facilities and contractors to the Commission. In this study the basic factors necessary to obtain quantitative cost delineation and evaluation have been outlined and some preliminary findings will be presented. The paper also presents a review of other economic studies made in the United States on particular process or facility applications. (author)

  1. Boll weevil (Coleoptera: Curculionidae) survival through the seed cotton cleaning process in the cotton gin.

    Science.gov (United States)

    Sappington, Thomas W; Brashears, Alan D; Parajulee, Megha N; Carroll, Stanley C; Arnold, Mark D; Baker, Roy V

    2004-08-01

    There is concern that gins located in boll weevil, Anthonomus grandis grandis Boheman, eradication zones may become points of reintroduction when they process cotton grown in a neighboring infested area. We estimated boll weevil survival through two typical machine sequences used in commercial cotton gins to clean and dry the seed cotton in advance of the gin stand, as well as separately through two incline cylinder cleaners or one or two tower dryers operating at different temperatures. Large numbers of laboratory-reared adult boll weevils were marked with fluorescent powder, fed into the test system, and recovered with the assistance of blacklights. We found no evidence of survival through the seed cotton cleaning systems even when the dryers were not heated, or when passed separately through the two incline cleaners alone. Upper confidence limits (95%) were calculated for the observed zero recoveries based on sample size and the binomial distribution, and these represent the statistical worst-case (i.e., highest) survival potential. Survival through heated tower dryers declined rapidly to zero at higher temperatures, especially when two dryers were running. Although we conclude that the potential for survival of weevils in the seed cotton to the gin stand is zero or close to zero, a small percentage of live weevils was recovered in the green boll/rock trap, which may represent the greatest threat of reintroduction at the gin. Escape of live weevils with the gin trash is also possible, and studies addressing this issue will be presented elsewhere. PMID:15384344

  2. An Experimental Study on Treatment of COD and TN in Nanofiltration Concentrate from Coking Wastewater with Fenton Oxidation Process%Fenton氧化法处理焦化纳滤浓水中COD及TN的研究

    Institute of Scientific and Technical Information of China (English)

    叶倩; 李恩超

    2016-01-01

    以焦化废水"三膜法"深度处理工艺产生的实际高电导率纳滤浓盐水为研究对象,考察不同PH值、Fe2+和H2O2条件下"芬顿法"去除焦化纳滤浓水中COD及TN的效率.%Deepened treatment of nanofiltration (NF) concentrated water with high con-ductivity from coking wastewater with three membranes method was studied. The efficiency of removing COD and total nitrogen (TN) from NF concentrate under different pH value, Fe2+and H202 condition by applying Fenton reagent oxidation process was investigated.

  3. 焦炉煤气配加转炉煤气生产甲醇工艺介绍%Methanol production process by coke oven gas and converter gas

    Institute of Scientific and Technical Information of China (English)

    熊江君; 吴映忠; 龙素安; 杨继涛

    2014-01-01

    This paper introduces the process and main technical characteristics of methanol produc -tion by coke oven gas and converter gas .This is a new usage of converter gas .The useful composition of fresh gas can be fully used.It has the advantages of high production rate and low energy consump -tion.%介绍了焦炉煤气配加转炉煤气生产甲醇的工艺流程及主要技术特点。该工艺开辟了利用转炉煤气的新方法,可充分利用新鲜气的有用成分,具有增产甲醇和降低消耗等优点。

  4. Multi-objective genetic algorithm for the optimization of road surface cleaning process

    Institute of Scientific and Technical Information of China (English)

    CHEN Jie; GAO Dao-ming

    2006-01-01

    The parameters affecting road surface cleaning using waterjets were researched and a fuzzy neural network method of calculating cleaning rate was provided. A genetic algorithm was used to configure the cleaning parameters of pressure, standoff distance, traverse rate and angle of nozzles for the optimization of the cleaning effectiveness, efficiency, energy and water consumption, and a multi-objective optimization model was established. After calculation, the optimized results and the trend of variation of cleaning effectiveness, efficiency, energy and water consumption in different weighting factors were analyzed.

  5. Cleaning Process Research of MVR High Concentration Salty Wastewater Treatment System

    Directory of Open Access Journals (Sweden)

    Wang Na

    2015-01-01

    Full Text Available A mechanical vapor re-compression (MVR evaporation system for the treatment of the highly-concentrated inorganic salt wastewater was investigated, and its process characteristics were analyzed taking sodium chloride salt wastewater as the treated solution. In this paper, by adding “H2O2 oxidation + filter +flash evaporation + hot filter” technology on the basis of original traditional MVR treatment system, the optimum technological conditions were determined through the experiment: The pH value is 8.5; the oxidation time is 24.0h; H2O2 amount accounting for 1% of the total wastewater under the condition of outlet test MVR system respectively fell 88.5% and 90.1% than the traditional process of effluent COD and NH3-N removal rate. MVR system for the sodium chloride salt qualified rate was increased from 83.2% to 98.2%. On the other hand, this process avoided the highly-concentrated outside of mother liquor by flashing evaporation recycling volatile solvent; the optimization process results were found to be consistent with published practical industrial data. Compared with the new process MVR system, the operation load of MVR system was lower. Therefore, the system can be used to treat the highly-concentrated inorganic salt wastewater and save energy. Therefore, the cleaning process can achieve remarkable energy saving and consumption, and reduce the pollution and the pollution and environmental protection effect.

  6. Coal and coke - analysis and testing. Determination of trace elements. Coal, coke and fly-ash. Determination of fluorine content. Pyrohydrolysis method

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    2001-06-29

    This Standard sets out a procedure for the pyrohydrolytic separation of fluorine from coal, coke and fly-ash and for determination of fluorine by gravimetric processing and either ion potentiometry or ion chromatography.

  7. Investigation of the timesaver process for de-burring and cleaning the plate for the Atlas Tilecalorimeter

    International Nuclear Information System (INIS)

    The Timesaver belt grinding machine has been selected by the Atlas collaboration for deburring the master and spacer plates after die stamping and laser cutting, respectively. However, the question has been raised as to whether or not the plates are sufficiently clean after going through the Timesaver machine to immediately be glued into a submodule assembly. This would greatly enhance the production of submodules because the task of cleaning individual master and spacer plates is labor intensive and time consuming as well as raises environmental issues with the detergent that is used. In order to investigate the possibility of using the Timesaver process to clean the plates as well as debur them, several plates were run through the machine and their cleanliness inspected before and after. In addition, several glue samples were subjected to the same process, glued, and then pulled apart in an attempt to gauge the cleanliness of the plates. From this series of tests it can be concluded that the wet Timesaver machine can adequately prepare the surface of the master and spacer plates as well as clean the plates for gluing. The machine was able to adequately remove all of the oil and grime from the test plates. Also, from the single test on the dry machine it appears that significant cleaning will be required to adequately clean the plates before gluing in order to remove the remaining grit

  8. Active biopolymers in green non-conventional media: a sustainable tool for developing clean chemical processes.

    Science.gov (United States)

    Lozano, Pedro; Bernal, Juana M; Nieto, Susana; Gomez, Celia; Garcia-Verdugo, Eduardo; Luis, Santiago V

    2015-12-21

    The greenness of chemical processes turns around two main axes: the selectivity of catalytic transformations, and the separation of pure products. The transfer of the exquisite catalytic efficiency shown by enzymes in nature to chemical processes is an important challenge. By using appropriate reaction systems, the combination of biopolymers with supercritical carbon dioxide (scCO2) and ionic liquids (ILs) resulted in synergetic and outstanding platforms for developing (multi)catalytic green chemical processes, even under flow conditions. The stabilization of biocatalysts, together with the design of straightforward approaches for separation of pure products including the full recovery and reuse of enzymes/ILs systems, are essential elements for developing clean chemical processes. By understanding structure-function relationships of biopolymers in ILs, as well as for ILs themselves (e.g. sponge-like ionic liquids, SLILs; supported ionic liquids-like phases, SILLPs, etc.), several integral green chemical processes of (bio)catalytic transformation and pure product separation are pointed out (e.g. the biocatalytic production of biodiesel in SLILs, etc.). Other developments based on DNA/ILs systems, as pathfinder studies for further technological applications in the near future, are also considered. PMID:26497761

  9. Coke from small-diameter tubes analyzed

    International Nuclear Information System (INIS)

    The mechanism for coke deposit formation and the nature of the coke itself can vary with the design of the ethylene furnace tube bank. In this article, coke deposits from furnaces with small-diameter pyrolysis tubes are examined. The samples were taken from four furnaces of identical design (Plant B). As in both the first and second installments of the series, the coke deposits were examined using a scanning electron microscope (SEM) and an energy dispersive X-ray analyzer (EDAX). The deposits from the small-diameter tubes are compared with the coke deposits from the furnace discussed in earlier articles. Analysis of the coke in both sets of samples are then used to offer recommendations for improved decoking procedures, operating procedures, better feed selection, and better selection of the metallurgy used in furnace tubes, to extend the operating time of the furnace tubes by reducing the amount and type of coke build up

  10. Bio-coke as an alternative to petroleum coke and metallurgical coke; Bio-cokes als alternatief voor petroleumcokes en metallurgische cokes

    Energy Technology Data Exchange (ETDEWEB)

    Croezen, H.J.; Van Lieshout, M. [CE Delft, Delft (Netherlands); Sevenster, M.N. [Sevenster Environmental Consultancy, Australian Capital Territory ACT (Australia)

    2012-11-15

    In the framework of elaborating the Dutch Roadmap Chemistry 2030), CE Delft has conducted an exploratory study for the Association of the Dutch Chemical Industry (VNCI) on the options of replacing (petroleum) coke in the chemical sector by biocokes. Coke is used as a reducing agent and/or raw material in four companies in the Dutch chemical industry (Tronox, ESD-SIC, Thermphos, Aluchemie). Replacing coke at these four companies can potentially yield a direct CO2 reduction of expectedly several hundreds of kilotons per year. For a first exploration of the options of bio-coke, CE Delft first conducted a desk study to get information on the quality and production costs for bio-coke. Subsequently, CE Delft had contact with the four chemical companies and a made a number of company visits. Moreover, the technical, economic and organizational capabilities, constraints and requirements with regard to a possible (partial) switch to biocokes have been explored. Based on the information available so far it can be concluded that biocokes seems to be a technically and economically interesting innovation. For implementation to finally take place, it is necessary to gain better insight in the technical and economic potential [Dutch] In verband met de uitwerking van de Routekaart Chemie 2030 heeft CE Delft voor VNCI een verkenning uitgevoerd naar de mogelijkheden voor vervanging van (petroleum)cokes in de chemische sector door biocokes. Cokes wordt gebruikt als reductiemiddel en/of grondstof bij een viertal bedrijven in de Nederlandse chemie (Tronox, ESD-SIC, Thermphos, Aluchemie). Het vervangen van cokes bij deze vier bedrijven kan in potentie een directe CO2-reductie van naar verwachting enkele honderden kilotonnen/jaar opleveren. Voor een eerste verkenning van de mogelijkheden van bio-cokes heeft CE Delft eerst een bureaustudie uitgevoerd naar informatie over kwaliteit van en productiekosten voor bio-cokes. Vervolgens heeft CE Delft contact gehad met de vier chemische

  11. The simulation of the hot boiler chemical clean (Siemens Process) in Pickering NGS 'B'

    International Nuclear Information System (INIS)

    A great insight of the most critical evolutions of the Hot Boiler Chemical Clean process prior to its application in PNGS 'B' was obtained with a number of models of the Heat Transport System. The simulated evolutions included the HTS warm up to a temperature of 170oC, HTS temperature and pressure control at 170oC and 4.1 MPa(a), respectively, with the Shutdown Cooling System operating in Warm Up Mode in conjunction with high Feed and Bleed flows and the Bleed Cooler, and the HTS pressure and temperature transients during the ASRVs venting of the Iron Step. Excellent agreement was obtained amongst the different numerical predictions and the data gathered during the actual HBCC of the Steam Generators of Unit 5. (author)

  12. Monte Carlo simulations of the clean and disordered contact process in three dimensions.

    Science.gov (United States)

    Vojta, Thomas

    2012-11-01

    The absorbing-state transition in the three-dimensional contact process with and without quenched randomness is investigated by means of Monte Carlo simulations. In the clean case, a reweighting technique is combined with a careful extrapolation of the data to infinite time to determine with high accuracy the critical behavior in the three-dimensional directed percolation universality class. In the presence of quenched spatial disorder, our data demonstrate that the absorbing-state transition is governed by an unconventional infinite-randomness critical point featuring activated dynamical scaling. The critical behavior of this transition does not depend on the disorder strength, i.e., it is universal. Close to the disordered critical point, the dynamics is characterized by the nonuniversal power laws typical of a Griffiths phase. We compare our findings to the results of other numerical methods, and we relate them to a general classification of phase transitions in disordered systems based on the rare region dimensionality. PMID:23214768

  13. Bench-scale testing of a micronized magnetite, fine-coal cleaning process

    Energy Technology Data Exchange (ETDEWEB)

    Suardini, P.J. [Custom Coals, International, Pittsburgh, PA (United States)

    1995-11-01

    Custom Coals, International has installed and is presently testing a 500 lb/hr. micronized-magnetite, fine-coal cleaning circuit at PETC`s Process Research Facility (PRF). The cost-shared project was awarded as part of the Coal Preparation Program`s, High Efficiency Preparation Subprogram. The project includes design, construction, testing, and decommissioning of a fully-integrated, bench-scale circuit, complete with feed coal classification to remove the minus 30 micron slimes, dense medium cycloning of the 300 by 30 micron feed coal using a nominal minus 10 micron size magnetite medium, and medium recovery using drain and rinse screens and various stages and types of magnetic separators. This paper describes the project circuit and goals, including a description of the current project status and the sources of coal and magnetite which are being tested.

  14. Cleaning the magnesium oxide contaminated stainless steel system using a high temperature decontamination process

    International Nuclear Information System (INIS)

    A high pressure and high temperature (HTHP) system made of stainless steel-316, that simulates the reactor coolant systems of pressurized water reactors has been constructed for carrying out experimental investigations on power reactor water chemistry. After two months of operation at 280 C, magnesium was observed in the coolant. This was attributed to the failure of some heater pins that contained magnesium oxide as insulator. This magnesium oxide got distributed over the entire system. In order to remove the magnesium that had deposited and reacted over the oxide film formed over the stainless steel surfaces, the system was chemically cleaned using a mixture of nitrilo-tri-acetic-acid (NTA) and N2H4 at high temperature. The chromium containing oxide film formed over the stainless steel surfaces are normally removed using oxidizing pretreatment followed by treatment with reducing formulation. A minimum of three such cycles are required to complete the dissolution of contaminated oxide film. It has been proved elsewhere that chromium-containing oxides can be dissolved by simple chelating agents but at a relatively higher temperature (150-180 C) with NTA. Thus, NTA based process was tested for its capability to remove the magnesium contaminated oxide film formed over stainless steel. In addition to stainless steel, the system has few carbon steel areas. Hence, the compatibility of stainless steel and carbon steel to the NTA-N2H4 mixture was determined. Tests were carried out at different concentrations of NTA and at different pH. It was observed that carbon steel corrosion rates were quite high at low pH. With increasing pH, the corrosion rate decreased. The surface roughening observed at low pH was not observed at pH 8.0. Hence, it was decided to carry out the cleaning at pH 7.0 and with NTA concentration of 5 mM. Visual examination of the test flanges after the cleaning indicated complete removal of the oxide film. Results of chemical analysis indicated that

  15. Influence of nut coke on iron ore sinter reducibility under simulated blast furnace conditions

    Energy Technology Data Exchange (ETDEWEB)

    Mousa, E.A.; Senk, D.; Babich, A.; Gudenau, H.W.

    2010-04-15

    One of the most important factors to increase the economic efficiency of the blast furnace process is to reduced coke losses (undersieve product known as nut coke). In recent years there has been increased interest in mixing nut coke in the sinter layers. In order to clarify the influence of nut coke on sinter reducibility, sinter and sinter-nut coke mixtures were isothermally reduced with 30%CO-70%N{sub 2} at 1173-1523 K using a muffle furnace supported by an on-line gas analyser. Reflected light microscopy, scanning electron microscopy and X-ray technique were used to characterise the microstructure and the different phases developed in the original and reduced sinter. Sinter reduced without nut coke participation exhibited reduction retardation at elevated temperatures (>1373 K) while the presence of nut coke prevented such phenomena. The rate controlling mechanism of sinter and sinter-nut coke mixture was predicted from the correlation between apparent activation energy calculations, mathematical modelling derived from gas-solid reaction model and microstructure examination.

  16. Parametric Study of Gasification of the Mexican Petroleum Coke: Effect Feed Petroleum Coke on Energetic Characteristic of the Synthetic Gas (syngas)

    OpenAIRE

    Longoria-Ramírez R.; González-Rocha J.C.; Urquiza-Beltrán G.

    2011-01-01

    In this work, a parametric study the gasification of the Mexican petroleum coke from the refineries of Cd Madero (CRM) and Cadereyta, Nuevo León (CRC) is performed. It is evaluates the energy behavior of the gasification process with objective to research which feedstock of petroleum coke has a be?? er yield of energy. Effect feed petroleum coke on energy characteristics of the clear synthetic gas (gasl): molar composition of CO and H2, High Heating Value (HHVgasl), energy power (Ogasl), Cold...

  17. Preperation for a Clean Surface

    OpenAIRE

    Aurimas Ralys; Valdemar Prokopovič; Vytautas Striška

    2013-01-01

    The article reviews techniques for preparing clean surfaces used in the manufacturing process, considers the types of clean surfaces and their role in modern production and provides the classification methods of arranging such surfaces. The paper also discusses the principles of methods for solvent cleaning, aqueous cleaning, ultrasonic cleaning, precision cleaning and mechanical cleaning. The study focuses on the possibility of adjusting a clean surface using a water flow, including cavitati...

  18. Preperation for a Clean Surface

    Directory of Open Access Journals (Sweden)

    Aurimas Ralys

    2012-12-01

    Full Text Available The article reviews techniques for preparing clean surfaces used in the manufacturing process, considers the types of clean surfaces and their role in modern production and provides the classification methods of arranging such surfaces. The paper also discusses the principles of methods for solvent cleaning, aqueous cleaning, ultrasonic cleaning, precision cleaning and mechanical cleaning. The study focuses on the possibility of adjusting a clean surface using a water flow, including cavitation.Article in Lithuanian

  19. A Medium-Scale 50 MWfuel Biomass Gasification Based Bio-SNG Plant: A Developed Gas Cleaning Process

    Directory of Open Access Journals (Sweden)

    Ramiar Sadegh-Vaziri

    2015-06-01

    Full Text Available Natural gas is becoming increasingly important as a primary energy source. A suitable replacement for fossil natural gas is bio-SNG, produced by biomass gasification, followed by methanation. A major challenge is efficient gas cleaning processes for removal of sulfur compounds and other impurities. The present study focuses on development of a gas cleaning step for a product gas produced in a 50 MWfuel gasification system. The developed gas cleaning washing process is basically a modification of the Rectisol process. Several different process configurations were evaluated using Aspen plus, including PC-SAFT for the thermodynamic modeling. The developed configuration takes advantage of only one methanol wash column, compared to two columns in a conventional Rectisol process. Results from modeling show the ability of the proposed configuration to remove impurities to a sufficiently low concentrations - almost zero concentration for H2S, CS2, HCl, NH3 and HCN, and approximately 0.01 mg/Nm3 for COS. These levels are acceptable for further upgrading of the gas in a methanation process. Simultaneously, up to 92% of the original CO2 is preserved in the final cleaned syngas stream. No process integration or economic consideration was performed within the scope of the present study, but will be investigated in future projects to improve the overall process.

  20. Membrane activated sludge process for cleaning industrial effluents; Membranbelebungsverfahren zur Reinigung industrieller Abwaesser

    Energy Technology Data Exchange (ETDEWEB)

    Cornel, P. [Institut WAR der Technischen Universitaet Darmstadt (Germany)

    2002-07-01

    The membrane activated sludge process provides a means of industrial effluent treatment which does full justice to the requirements of high product quality, low space requirement, modular design and extensibility. The product is free of solids and largely free of pathogens. It can either be used directly as industrial water or treated further by means of nanofiltration or reverse osmosis to yield process water. Besides saving costs this can make a significant contribution to the conservation of resources. The membrane activated sludge process has been realised at an industrial scale in many branches of industry, providing many years of operating experience. However, experience has shown that some types of wastewater are apparently unsuitable for the membrane activated sludge process. These are characterised by low, rapidly decreasing throughput rates (fluxes) and a need for costly cleaning techniques. [German] Mit dem Membranbelebungsverfahren steht eine Verfahrensvariante zur industriellen Abwasserreinigung zur Verfuegung, mit der sich die Forderungen nach hoher Ablaufqualitaet, geringem Platzbedarf, modularem Aufbau und Erweiterbarkeit realisieren lassen. Der Ablauf ist feststofffrei und keimarm und kann ggf. direkt als Brauchwasser genutzt oder mittels Nanofiltration oder Umkehrosmose zu Prozesswasser aufbereitet werden. Dies kann erheblich zur Ressourcenschonung beitragen und zudem wirtschaftlich vorteilhaft sein. Das Membranbelebungsverfahren ist in etlichen Branchen grosstechnisch realisiert. Mehrjaehrige Betriebserfahrungen liegen mittlerweile vor. Die Erfahrung zeigt aber auch, dass es Abwaesser gibt, die offenbar ungeeignet fuer das Membranbelebungsverfahren sind. Niedrige, schnell abnehmende Durchsaetze (Flux, Fluss) und ein hoher Reinigungsaufwand sind kennzeichnend fuer solche Abwaesser. (orig.)

  1. Clean coal technology

    International Nuclear Information System (INIS)

    Coal is the major source of energy in India at present as well as in foreseeable future. With gradual deterioration in coal quality as well as increased awareness on environmental aspects, clean coal technologies have to be adopted by major coal consuming sectors. The probable routes of restricting environmental degradation in power generation include beneficiation of power coal for maintaining consistency in coal supply and reducing pollutant emission, adoption of fluidized bed combustion on a larger scale, adoption of technologies for controlling SOx and NOx emission during and after combustion, adoption of larger capacity and improved and non-recovery type coke ovens

  2. Mathematical model of dust cleaning process in centrifugal-inertial dust collector

    OpenAIRE

    Batluk, V.; Paranyak, N.; Makarchuk, V.

    2013-01-01

    The article is devoted to the problem of providing air cleaning from dust in various industries, using highly efficient apparatus, with the aim of bringing the volume of harmful emissions to the sanitary standards. The article presents new directions in creating of dust cleaning apparatus, based on the usage of centrifugal, inertial forces, by which the efficiency of dust collection could be significantly increased.

  3. Method to obtain sulphur from the hydrogen sulphide of coke oven gas with simultaneous combustion of the coke oven gas ammonia

    Energy Technology Data Exchange (ETDEWEB)

    Wunderlich, G.; Weber, H.

    1976-02-05

    The invention deals with a method to obtain sulphur from coke oven gas hydrogen sulphide by partly combusting to sulphur dioxide and processing to sulphur with simultaneous combustion of the coke oven ammonia according to the Claus method. The method is thus characterized in that the ammonia combustion gases released from the heating boiler are after cooling freed from the aqueous condensate and then are added to the partly combusted hydrogen sulphide clouds before introducing into the Claus oven system.

  4. Recovery of reagent in a process for producing ultra clean coal

    Energy Technology Data Exchange (ETDEWEB)

    K.M. Steel; J.W. Patrick [Nottingham University, Nottingham (United Kingdom). Nottingham Fuel and Energy Centre

    2003-07-01

    A technique for selectively separating approximately 65 wt% of the Si(IV) in coal has been developed. The technique first uses aqueous HF to react with aluminosilicates and quartz to form fluoride complexed Al and Si species in solution. Aluminium cations, in the form of Al(NO{sub 3}){sub 3}, are then added to the solution to complex fluoride as AlF{sub 2}{sup +} and hydrolyse the silicon fluoride species to silicon hydroxide, which precipitates as pure silica gel and is removed by filtration. The solution is then distilled to recover a water stream, a nitric acid stream and a solid residue. The water stream is used to pyrohydrolyse the solid residue at temperatures in excess of 500{sup o}C to liberate HF for recycling. To complete the circuit, the solid remaining after pyrohydrolysis is treated with the nitric acid stream to produce Al(NO{sub 3}){sub 3} for recycling. The application of this work is primarily as part of a process for producing ultra-clean coal. As it is a technique for the selective separation of Al and Si from aluminosilicates, it may have application in other areas of mineral processing. 10 refs., 3 figs., 2 tabs.

  5. Development of coke oven combustion control technology (I): combustion characteristics of coke in the vertical direction

    Energy Technology Data Exchange (ETDEWEB)

    Tamura, Y.; Yamamoto, T.; Katayama, A.; Takase, S.; Okui, N.

    1983-01-01

    Measurements of the temperature distribution in a coking chamber and sampling plus analysis of the product coke have confirmed that temperature fluctuations in the upper coking chamber of a single-stage burner type oven (such as a Koppers oven) have a large effect on the variations of coke quality. Control of such temperature fluctuations is therefore essential. A possible computerized combustion control system for improving temperature control is described. 2 references.

  6. Final Report of NATO/SPS Pilot Study on Clean Products and Processes (Phase I and II)

    Science.gov (United States)

    Early in 1998 the NATO Committee for Challenges to Modern Society (SPS) (Science for Peace and Security) approved the Pilot Study on Clean Products and Processes for an initial period of five years. The pilot was to provide a forum for member country representatives to discuss t...

  7. The microbial ecology of processing equipment in different fish industries-analysis of the microflora during processing and following cleaning and disinfection.

    Science.gov (United States)

    Bagge-Ravn, Dorthe; Ng, Yin; Hjelm, Mette; Christiansen, Jesper N; Johansen, Charlotte; Gram, Lone

    2003-11-01

    The microflora adhering to the processing equipment during production and after cleaning and disinfecting procedures was identified in four different processing plants. A total of 1009 microorganisms was isolated from various-agar plates and identified. A stepwise procedure using simple phenotypic tests was used to identify the isolates and proved a fast way to group a large collection of microorganisms. Pseudomonas, Neisseriaceae, Enterobactericeae, Coryneform, Acinetobacter and lactic acid bacteria dominated the microflora of cold-smoked salmon plants, whereas the microflora in a plant processing semi-preserved herring consisted of Pseudomonas, Alcaligenes and Enterobactericeae. Psychrobacter, Staphylococcus and yeasts were found in a caviar processing plant. Overall, many microorganisms that are often isolated from fish were also isolated from the fish processing plants. However, some selection depending on processing parameters occurred, since halo- and osmo-tolerant organisms dominated in the caviar processing. After cleaning and disinfection, yeasts, Pseudomonas, Neisseriaceae and Alcaligenes remained in smokehouses, yeasts and Pseudomonas in the herring plant and Pseudomonas, Staphylococcus and yeasts in the caviar plant. The dominant adhering organisms after cleaning and disinfection were pseudomonads and yeasts independently of the microflora during processing. Knowledge of the adhering microflora is essential in the Good Hygienic Practises programme of food processing plants, as the development and design of improved cleaning and disinfecting procedures should target the microorganisms persisting and potentially contaminating the product. PMID:14527796

  8. The world coke market. Problems and outlook

    International Nuclear Information System (INIS)

    Outlooks to the world coke market are considered with regard to supply and demand as well as the current state of capacities for its production in some countries of Asia, Western and Eastern Europe, USA. In experts opinion increase of coke import from China, increase in service life of currently operating coke furnaces, as well as more extensive use of PCI coal mixture are among the most feasible opportunities for its Western consumers

  9. Application of 150t/h coke dry quenching technique in Bengang coke oven%150t/h干熄焦在本钢焦炉的应用

    Institute of Scientific and Technical Information of China (English)

    全喜红

    2009-01-01

    The main process of 150t/h coke dry quenching technique in Bengang No. 6 and 7 coke oven were introduced. According to actual operation data, the environmental protection effect and energy saving characteristic of coke dry quenching technology were analyzed. It will be of great importance in the application and dissemination of coke dry quenching technology, especially that of Chinese property.%介绍了本钢6、7号焦炉干熄焦的主要工艺流程,通过实际数据详细分析了干熄焦运行的节能效益及环保效应,对国内干熄焦技术推广与应用将起到积极的推动作用.

  10. Optimization of the process of steel strip perforation and nickel platting for the purpose of elimination of trichloroethylene from the cleaning process of perforated steel strip

    Directory of Open Access Journals (Sweden)

    Petrović Aleksandra B.

    2009-01-01

    Full Text Available In the production of pocket type electrodes for Ni-Cd batteries perforation of proper steel strips and then nickel platting of perforated steel strips were made. In the nickel platting process, the organic solvent, trichloroethylene, has previously been used for cleaning. Due to the carcinogenic nature of trichloroethylene and the many operations previously required during cleaning, it was considered to do cleaning of perforated steel strips without use of the mentioned organic solvent. In the purpose of elimination of trichloroethylene from the cleaning process of perforated steel strips, the tests of perforation of steel strips with use of oils of different viscosity were made. It was shown that there was no dysfunction during the work of the perforation plants, meaning there was no additional heating of the strips, deterring of the steel filings, nor excessive wearing of the perforation apparatus. The perforation percent was the same irrelevant of the viscosity of the used oil. Before being perforated using the oils with different viscosity, the nickel platting steel strips were cleaned in different degreasers (based on NaOH as well as on KOH. It was shown that efficient cleaning without the use of trichloroethylene is possible with the use of oil with smaller viscosity in the perforated steel strips process and the degreaser based on KOH in the cleaning process, before nickel platting. It also appeared that the alkali degreaser based on KOH was more efficient, bath corrections were made less often and the working period of the baths was longer, which all in summary means less quantity of chemicals needed for degreasing of perforated steel strips.

  11. A heating partition for a coking furnace

    Energy Technology Data Exchange (ETDEWEB)

    Strelov, K.K.; Ivanova, A.V.; Kaufman, A.A.; Kuznetsov, G.I.; Likhogub, Ye.P.; Turman, D.S.; Varshavskiy, T.P.; Volfovskiy, G.M.

    1983-01-01

    A coking furnace heating partition (OPKT) is proposed in order to increase reliability by increasing its strength. The proposal includes equipping with a vertical wall (St) made of Dinas brick and positioning it along the longitudinal axis of the coking furnace heating panel. The dividing walls are made of Dinas brick and their faces are disposed between the bricks of the wall of the coking chamber (KK). The surface of the coking chamber wall is made from magnesite or corundum brick which makes up 70 to 80 percent of the operational surface (Pv) of the wall. The presence of the vertical wall in combination with the

  12. Investigation on activated semi-coke desulfurization

    Institute of Scientific and Technical Information of China (English)

    SHANGGUAN Ju; LI Zhuan-li; LI Chun-hu

    2005-01-01

    An activated semi-coke with industrial-scale size was prepared by high-pressure hydrothermal chemistry activation, HNO3oxidation and calcination activation in proper order from Inner Mongolia Zhalainuoer semi-coke, which is rich in resource and cheap in sale.SO2 adsorption capacity on this activated semi-coke was assessed in the fixed bed in the temperature range of 60-170℃, space velocity range of 500-1300 h-1, SO2 concentration of 1000-3000 ppmv, and N2 as balance. The surface area, elemental and proximate analysis for both raw semi-coke and activated semi-cokes were measured. The experimental results showed that the activated semi-coke has a high adsorption capacity for sulfur dioxide than the untreated semi-coke. This may be the result of increase of surface area on activated semi-coke and surface oxygen functional groups with basicity characteristics. Comparison to result of FTIR, it is known that group of-C-O-C- may be active center of SO2 catalytic adsorption on activated semi-coke.

  13. Well-ordered polymer nano-fibers with self-cleaning property by disturbing crystallization process

    Science.gov (United States)

    Yang, Qin; Luo, Zhuangzhu; Tan, Sheng; Luo, Yimin; Wang, Yunjiao; Zhang, Zhaozhu; Liu, Weimin

    2014-07-01

    Bionic self-cleaning surfaces with well-ordered polymer nano-fibers are firstly fabricated by disturbing crystallization during one-step coating-curing process. Orderly thin (100 nm) and long (5-10 μm) polymer nano-fibers with a certain direction are fabricated by external macroscopic force ( F blow) interference introduced by H2 gas flow, leading to superior superhydrophobicity with a water contact angle (WCA) of 170° and a water sliding angle (WSA) of 0-1°. In contrast, nano-wires and nano-bridges (1-8 μm in length/10-80 nm in width) are generated by "spinning/stretching" under internal microscopic force ( F T) interference due to significant temperature difference in the non-uniform cooling medium. The findings provide a novel theoretical basis for controllable polymer "bionic lotus" surface and will further promote practical application in many engineering fields such as drag-reduction and anti-icing.

  14. The Evolution of Structural Order as a Measure of Thermal History of Coke in the Blast Furnace

    Science.gov (United States)

    Lundgren, Maria; Khanna, Rita; Ökvist, Lena Sundqvist; Sahajwalla, Veena; Björkman, Bo

    2014-04-01

    Investigations were carried out on cokes heat treated in the laboratory and on cokes extracted from the experimental blast furnace (EBF) raceway and hearth. X-ray diffraction (XRD) measurements were performed to investigate changes in structural order ( L c), chemical transformations in coke ash along with comparative thermodynamic equilibrium studies and the influence of melt. Three data processing approaches were used to compute L c values as a function of temperature and time and linear correlations were established between L c and heat treatment temperatures during laboratory investigations. These were used to estimate temperatures experienced by coke in various regions of EBF and estimated raceway temperatures were seen to follow the profile of combustion peak. The MgAl2O4 spinel was observed in coke submerged in slag during laboratory studies and in cokes found further into the raceway. Coke in contact with hot metal showed XRD peaks corresponding to presence of Fe3Si. The intensity of SiO2 peak in coke ash was seen to decrease with increasing temperature and disappeared at around 1770 K (1500 °C) due to the formation of SiC. This study has shown that the evolution of structural order and chemical transformations in coke could be used to estimate its thermal history in blast furnaces.

  15. Zeolite deactivation during hydrocarbon reactions: characterisation of coke precursors and acidity, product distribution

    OpenAIRE

    Wang, B.

    2008-01-01

    The catalytic conversion of hydrocarbons over zeolites has been applied in large scale petroleum-refining processes. However, there is always formation and retention of heavy by-products, called coke, which causes catalyst deactivation. This deactivation is due to the poisoning of the acid sites and/or pore blockage. The formation of coke on hydrocarbon processing catalysts is of considerable technological and economic importance and a great deal of work has been carried out to this study. Th...

  16. Factors affecting the microwave coking of coals and the implications on microwave cavity design

    OpenAIRE

    Binner, Eleanor; Medeira-Munoyerro, Maria; Huddle, Thomas; Kingman, S. W.; Dodds, Chris; Dimitrakis, G.; Robinson, John P.; Lester, Edward

    2014-01-01

    The work carried out in this paper assessed how processing conditions and feedstock affect the quality of the coke produced during microwave coke making. The aim was to gather information that would support the development of an optimised microwave coke making oven. Experiments were carried out in a non-optimised 2450 MHz cylindrical cavity. The effect of treatment time (15–120 min), power input (750 W–4.5 kW) and overall power input (1700–27,200 kWh/t) on a range of coals (semi-bituminous–an...

  17. Integrated hot fuel gas cleaning for advanced gasification combined cycle process

    Energy Technology Data Exchange (ETDEWEB)

    Nieminen, M.; Kangasmaa, K.; Laatikainen, J.; Staahlberg, P.; Kurkela, E. [VTT Energy, Espoo (Finland). Gasification and Advanced Combustion

    1996-12-01

    The fate of halogens in pressurised fluidized-bed gasification and hot gas filtration is determined. Potential halogen removal sorbents, suitable for integrated hot gas cleaning, are screened and some selected sorbents are tested in bench scale. Finally, halogen removal results are verified using the PDU-scale pressurised fluidized-bed gasification and integrated hot gas cleaning facilities of VTT. The project is part of the JOULE II Extension programme of the European Union. (author)

  18. Photoluminescence study of GaAs homoepitaxial structures with different in situ substrate surface cleaning processes

    OpenAIRE

    Javier Luyo-Alvarado; Miguel Meléndez-Lira; Máximo López-López; Shigeo Goto

    1997-01-01

    We have studied the substrate-film interface of GaAs homoepitaxial structures prepared by molecular beam epitaxy, employing three different in situ treatments for the substrate surface preparation: 1) Cleaning by hydrogen radicals (H*), 2) Exposure to trisdimethylaminoarsine (TDMAAs), and 3) The usual thermal cleaning under an arsenic flux. The concentrations of interfacial residual impurities of C and O were measured by secondary ion mass spectroscopy (SIMS). For semi-insulating substrates, ...

  19. Experimental investigations of ammonia adsorption and nitric oxide reduction on activated coke

    Energy Technology Data Exchange (ETDEWEB)

    Sirko Ogriseck; Gloria Patricia Galindo Vanegas [Infraserv GmbH & Co. Hoechst KG, Frankfurt am Main (Germany)

    2010-06-01

    In this work the enhancement of ammonia adsorption on activated coke has been investigated to increase the efficiency of the denitrification in the dry flue gas cleaning system located at Infraserv GmbH & Co. Hoechst KG in Frankfurt am Main, Germany. The influence of loading temperatures and sulfur components content of the activated coke on the ammonia adsorption were studied. Additionally, urea was tested as an alternative loading substance. Increasing ammonia adsorption was observed by raising loading temperatures. The highest ammonia loading was possible at the highest temperature tested at 469{sup o}C. The activated coke loaded at these conditions, as well as the one loaded with urea, was found to have higher denitrification efficiency than that loaded at present conditions of about 114{sup o}C. The results of this study allowed the recommendation of possible measures to be applied in the plant to increase its denitrification efficiency.

  20. Preparation of modified semi-coke by microwave heating and adsorption kinetics of methylene blue.

    Science.gov (United States)

    Wang, Xin; Peng, Jin-Hui; Duan, Xin-Hui; Srinivasakannan, Chandrasekar

    2013-01-01

    Preparation of modified semi-coke has been achieved, using phosphoric acid as the modifying agent, by microwave heating from virgin semi-coke. Process optimization using a Central Composite Design (CCD) design of Response Surface Methodology (RSM) technique for the preparation of modifies semi-coke is presented in this paper. The optimum conditions for producing modified semi-coke were: concentration of phosphoric acid 2.04, heating time 20 minutes and temperature 587 degrees C, with the optimum iodine of 862 mg/g and yield of 47.48%. The textural characteristics of modified semi-coke were analyzed using scanning electron microscopy (SEM) and nitrogen adsorption isotherm. The BET surface area of modified semi-coke was estimated to be 989.60 m2/g, with the pore volume of 0.74 cm3/g and a pore diameter of 3.009 nm, with micro-pore volume contributing to 62.44%. The Methylene Blue monolayer adsorption capacity was found to be mg/g at K. The adsorption capacity of the modified semi-coke highlights its suitability for liquid phase adsorption application with a potential usage in waste water treatment. PMID:24779145

  1. KRESS INDIRECT DRY COOLING SYSTEM, BETHLEHEM STEEL'S COKE PLANT DEMONSTRATION AT SPARROWS POINT, MARYLAND - VOLUME 2. APPENDICES G-N

    Science.gov (United States)

    The report evaluates the Kress Indirect Dry Cooling (KIDC) process, an innovative system for handling and cooling coke produced from a slot-type by-product coke oven battery. The report is based on the test work and demonstration of the system at Bethlehem Steel Corporation's Sp...

  2. Pre-commissioning of 120 kt/a Unit for Hydrotreating Crude Coke Oven Benzene Implemented at Baoyuan Chemical Company

    Institute of Scientific and Technical Information of China (English)

    2008-01-01

    @@ The Baoyuan Chemical Company, Ltd. in Taiyuan has per-formed the precommissioning of a 120 kt/a unit for hydrotreating crude coke oven benzene. This unit is the phase II construction of the 300 kt/a crude benzene hydrotreating project, which adopts the process technology for hydrotreating crude coke oven benzene developed indepen-dently by our own efforts.

  3. Dry Cleaning

    OpenAIRE

    Shirley, Lindsey; Weller, Chanae

    2010-01-01

    Despite its name, commercial dry cleaning is not actually a “dry” process. Clothes are immersed in a solvent, most commonly perchlorethylene (perc), instead of in water. Perc or other similar solvents are effective in the removal of oil and grease-based stains without damaging or shrinking sensitive fabrics, unlike a regular detergents and fabric softeners.

  4. Rapid formation of phase-clean 110 K (Bi-2223) powders derived via freeze-drying process

    Science.gov (United States)

    Balachandran, Uthamalingam

    1996-01-01

    A process for the preparation of amorphous precursor powders for Pb-doped Bi.sub.2 Sr.sub.2 Ca.sub.2 Cu.sub.3 O.sub.x (2223) includes a freeze-drying process incorporating a splat-freezing step. The process generally includes splat freezing a nitrate solution of Bi, Pb, Sr, Ca, and Cu to form flakes of the solution without any phase separation; grinding the frozen flakes to form a powder; freeze-drying the frozen powder; heating the dried powder to form a dry green precursor powders; denitrating the green-powders; heating the denitrated powders to form phase-clean Bi-2223 powders. The grain boundaries of the 2223 grains appear to be clean, leading to good intergrain contact between 2223 grains.

  5. Color and chlorinated organics removal from pulp mills wastewater using activated petroleum coke.

    Science.gov (United States)

    Shawwa, A R; Smith, D W; Sego, D C

    2001-03-01

    Delayed petroleum coke, a waste by-product from the oil sand industry, was utilized in the production of activated carbon. The activated carbon was then evaluated for color and chlorinated organics reduction from pulp mill wastewater. The activation of the petroleum coke was evaluated using a fixed bed reactor involving carbonization and activation steps at temperature of 850 degrees C and using steam as the activation medium. The activation results showed that the maximum surface area of the activated coke was achieved at an activation period of 4 h. The maximum surface area occurred at burnoff and water efficiency of 48.5 and 54.3%, respectively. Increasing the activation period to 6 h resulted in a decrease in the surface area. Methylene blue adsorption results indicated that the activation process was successful. Methylene blue adsorbed per 100 g of applied activated coke was 10 times higher than that adsorbed by raw petroleum coke. Adsorption equilibrium results of the bleached wastewater and the activated coke showed that significant color, COD, DOC and AOX removal (> 90%) was achieved when the activated coke dose exceeded 15,000 mg/L. Adsorption isotherms, in terms of COD, DOC, UV and color were developed based on the batch equilibrium data. Based on these isotherms, the amount of activated coke required to achieve certain removal of color and AOX can be predicted. The utilization of the petroleum coke for the production of activated carbon can provide an excellent disposal option for the oil sand industry at the same time would provide a cheap and valuable activated carbon. PMID:11228973

  6. Methanol gasoline blend from petroleum coke sources

    Energy Technology Data Exchange (ETDEWEB)

    Netzer, David [Consulting Chemical Engineer (United States); Wallsgrove, Chris [Process Engineering Manager (United States)

    2011-07-01

    In Alberta, a large amount of petroleum coke is produced as a byproduct from processes relating to bitumen upgrading and refining. Unfortunately, there is little to no market for this product in the province. This presentation addresses concerns relating to the concept of converting the otherwise wasted petcoke into methanol and using it as a blending component in gasoline. The presentation tackles issues relating to environmental impact, economics, renewability, toxicity, safety, and vehicle design by analyzing and comparing the proposed methanol/gasoline (M-10) to that of an ethanol/gasoline (E-10). The presentation covers analysis of the CO2 emissions, an analysis of the finances, and a number of scenarios involving the improper use or accidental spillage of M-10. Through the comparison of methanol/gasoline and ethanol/gasoline, the presentation demonstrated that converting the petcoke byproduct into methanol for use as a gasoline blend is a viable option.

  7. Production of conductive coke for cathodic protection

    Energy Technology Data Exchange (ETDEWEB)

    Mogollon, E.G.; Henao, L.E.; Pacheco, L.A.; Ortiz, J.L.; Diaz, J.J. [Universidad Nacional de Colombia, Bogota (Colombia). Departamento de Quimica

    1999-07-01

    The reduction of resistivity of coke by means of the cocarbonization of mixtures of coking coals was studied using coal tar as an additive. Optimum temperature and blending conditions for decreased resistivity were investigated. The effect of particle size on the dependency of coal rank was investigated. 2 refs., 4 figs., 2 tabs.

  8. Neutron probe monitoring of water in coke

    International Nuclear Information System (INIS)

    Coke moisture ranges between 5 and 7%. At coke sampling, inaccuracies occur in water content assessment. The results alter depending on hourly and daily samples and on sampling points. In the blast furnace situation where the knowledge of coke moisture is important for determining specific consumption of coke, the neutron moisture gauge continuous method has been proven. The effect was studied of different contents of volatile compounds in coke, as were the effects of the types of steel and the wall thickness of the neutron probe protective tube and those of big lumps of coke and of anomalous moisture on determination accuracy. The neutron probe operation may also be affected by bulk density and by consistency of the coke granulometric composition. The steel protective tube should be made of a strong material guaranteeing long-term invariability of measuring conditions. Mixing should not take place of compacting and bulk operation coke. Under these conditions, measurement can be sufficiently accurate. (M.D.). 2 tabs., 1 fig., 5 refs

  9. CARCINOGEN ASSESSMENT OF COKE OVEN EMISSIONS

    Science.gov (United States)

    Coke oven workers in Allegheny County, Pennsylvania and at 10 non-Allegheny County coke plants in the United States and Canada were found to be at an excess risk of mortality from cancer of all sites and from cancer of the lungs, bronchus, trachea, kidney, and prostate. An import...

  10. Morphological stability of the atomically clean surface of silicon (100) crystals after microwave plasma-chemical processing

    International Nuclear Information System (INIS)

    The morphological stability of atomically clean silicon (100) surface after low-energy microwave plasma-chemical etching in various plasma-forming media is studied. It is found that relaxation changes in the surface density and atomic bump heights after plasma processing in inert and chemically active media are multidirectional in character. After processing in a freon-14 medium, the free energy is minimized due to a decrease in the surface density of microbumps and an increase in their height. After argon-plasma processing, an insignificant increase in the bump density with a simultaneous decrease in bump heights is observed. The physicochemical processes causing these changes are considered

  11. Morphological stability of the atomically clean surface of silicon (100) crystals after microwave plasma-chemical processing

    Energy Technology Data Exchange (ETDEWEB)

    Yafarov, R. K., E-mail: pirpc@yandex.ru; Shanygin, V. Ya. [Russian Academy of Sciences, Saratov Branch of the Kotel’nikov Institute of Radio Engineering and Electronics (Russian Federation)

    2016-01-15

    The morphological stability of atomically clean silicon (100) surface after low-energy microwave plasma-chemical etching in various plasma-forming media is studied. It is found that relaxation changes in the surface density and atomic bump heights after plasma processing in inert and chemically active media are multidirectional in character. After processing in a freon-14 medium, the free energy is minimized due to a decrease in the surface density of microbumps and an increase in their height. After argon-plasma processing, an insignificant increase in the bump density with a simultaneous decrease in bump heights is observed. The physicochemical processes causing these changes are considered.

  12. Recycling of Coking Plant Residues in a Finnish Steelworks—Laboratory Study and Replacement Ratio Calculation

    OpenAIRE

    Suopajärvi, Hannu; Salo, Antti; Paananen, Timo; Mattila, Riku; Fabritius, Timo

    2013-01-01

    Material efficiency is one of the most effective methods for achieving more sustainable operations in iron and steelmaking. Sintering and briquetting processes are commonly used in integrated steel plants to recycle carbon- and iron-containing residues back to blast furnace. In the Ruukki steelworks in Finland, a surplus of solid coking plant by-products is produced, none of which are presently utilized within the steelworks. In this paper, a novel concept for recycling solid coking plant by-...

  13. Digital processing of SEM images for the assessment of evaluation indexes of cleaning interventions on Pentelic marble surfaces

    International Nuclear Information System (INIS)

    In this work, digital processing of scanning-electron-microscopy images utilized to assess cleaning interventions applied on the Pentelic marble surfaces of the National Archaeological Museum and National Library in Athens, Greece. Beside mineralogical and chemical characterization that took place by scanning-electron-microscopy with Energy Dispersive X-ray Spectroscopy, the image-analysis program EDGE was applied for estimating three evaluation indexes of the marble micro-structure. The EDGE program was developed by the U.S. Geological Survey for the evaluation of cleaning interventions applied on Philadelphia City Hall. This computer program analyzes scanning-electron-microscopy images of stone specimens cut in cross-section for measuring the fractal dimension of the exposed surfaces, the stone near-surface fracture density, the shape factor (a surface roughness factor) and the friability index which represents the physico-chemical and physico-mechanical stability of the stone surface. The results indicated that the evaluation of the marble surface micro-structure before and after cleaning is achieved by the suggested indexes, while the performance of cleaning interventions on the marble surfaces can be assessed

  14. FY1995 development of a clean CVD process by evaluation and control of gas phase nucleation phenomena; 1995 nendo kisokaku seisei gensho no hyoka to seigyo ni yoru clean CVD process no kaihatsu

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1997-03-01

    The purpose of this study is to develop a high-rate and clean chemical vapor deposition (CVD) process as a breakthrough technique to overcome the problems that particles generated in the gas phase during CVD process for preparation of functional thin films cause reduced product yield and deterioration of the films. In the CVD process proposed here, reactant gas and generated particles are electrically charged to control the motion of them with an electric field. In this study, gas-phase nucleation phenomena are evaluated both theoretically and experimentally. A high-rate, ionized CVD method is first developed, in which reactant gas and generated particles are charged with negative ions generated from a radioisotope source and the UV/photoelectron method, and the motion of the charged gas and particles is controlled with an electric field. Charging and transport processes of fine particles are then investigated experimentally and theoretically to develop a clean CVD method in which generated particles are removed with the electric forces. As a result, quantitative evaluation of the charging and transport process was made possible. We also developed devices for measuring the size distribution and concentration of fine particles in low pressure gas such as those found in plasma CVD processes. In addition, numerical simulation and experiments in this study for a TEOS/O{sub 3} CVD process to prepare thin films could determine reaction rates which have not been known so far and give information on selecting good operation conditions for the process. (NEDO)

  15. Emissions of polycyclic aromatic hydrocarbons from coking industries in China

    Institute of Scientific and Technical Information of China (English)

    Ling Mu; Lin Peng; Junji Cao; Qiusheng He; Fan Li; Jianqiang Zhang; Xiaofeng Liu

    2013-01-01

    This study set out to assess the characteristics of polycyclic aromatic hydrocarbon (PAH) emission from coking industries,with field samplings conducted at four typical coke plants.For each selected plant,stack flue gas samples were collected during processes that included charging coal into the ovens (CC),pushing coke (PC) and the combustion of coke-oven gas (CG).Sixteen individual PAHs on the US EPA priority list were analyzed by gas chromatography/mass spectrometry (GC/MS).Results showed that the total PAH concentrations in the flue gas ranged from 45.776 to 414.874 μg/m3,with the highest emission level for CC (359.545 μg/m3).The concentration of PAH emitted from the CC process in CP1 (stamp charging) was lower than that from CP3 and CP4 (top charging).Low-molecular-weight PAHs (i.e.,two-to three-ring PAHs) were predominant contributors to the total PAH contents,and Nap,AcPy,Flu,PhA,and AnT were found to be the most abundant ones.Total BaPeq concentrations for CC (2.248 iμg/m3) were higher than those for PC (1.838 μg/m3) and CG (1.082 μg/m3),and DbA was an important contributor to carcinogenic risk as BaP in emissions from coking processes.Particulate PAH accounted for more than 20% of the total BaPeq concentrations,which were significantly higher than the corresponding contributions to the total PAH mass concentration (5%).Both particulate and gaseous PAH should be taken into consideration when the potential toxicity risk of PAH pollution during coking processes is assessed.The mean total-PAH emission factors were 346.132 and 93.173 μg/kg for CC and PC,respectively.

  16. Computational study of a self-cleaning process on superhydrophobic surface

    Science.gov (United States)

    Farokhirad, Samaneh

    All substances around us are bounded by interfaces. In general, interface between different phases of materials are categorized as fluid-fluid, solid-fluid, and solid-solid. Fluid-fluid interfaces exhibit a distinct behavior by adapting their shape in response to external stimulus. For example, a liquid droplet on a substrate can undergo different wetting morphologies depending on topography and chemical composition of the surface. Fundamentally, interfacial phenomena arise at the limit between two immiscible phases, namely interface. The interface dynamic governs, to a great extent, physical processes such as impact and spreading of two immiscible media, and stabilization of foams and emulsions from break-up and coalescence. One of the recent challenging problems in the interface-driven fluid dynamics is the self-propulsion mechanism of droplets by means of different types of external forces such as electrical potential, or thermal Marangoni effect. Rapid removal of self-propelled droplet from the surface is an essential factor in terms of expense and efficiency for many applications including self-cleaning and enhanced heat and mass transfer to save energy and natural resources. A recent study on superhydrophobic nature of micro- and nanostructures of cicada wings offers a unique way for the self-propulsion process with no external force, namely coalescence-induced self-propelled jumping of droplet which can act effectively at any orientation. The biological importance of this new mechanism is associated with protecting such surfaces from long term exposure to colloidal particles such as microbial colloids and virus particles. Different interfacial phenomena can occur after out-of-plane jumping of droplet. If the departed droplet is landed back by gravity, it may impact and spread on the surface or coalesce with another droplet and again self-peopled itself to jump away from the surface. The complete removal of the propelled droplet to a sufficient distance

  17. Inhibition of the Nitrification Process of Activated Sludge Micro-Organism by Scrubber Water from an Industrial Flue Gas Cleaning Process

    DEFF Research Database (Denmark)

    Thomsen, Jens Peter

    2007-01-01

    The microbial transformation of ammonia to nitrate, the nitrification, is a central process in the nitrogen biogeochemical cycle. In a modern wastewater treatment plant, the nitrification process is a key process in the removal of nitrogen and inhibitory compounds in sewage can seriously affect the...... nitrogen removal. A major sewage cleaning plant in the southern part of Denmark is a recipient of industrial sewage from a major fish meal industry. Severe nitrification inhibition was observed in scrubber water from an incineration of process air, and the processes that lead to the production were stopped...... using active sludge from the municipal wastewater cleaning plant. The investigation showed that it is possible to reduce the nitrification inhibition effect considerably by raising the incineration temperature from 800°C to 850°C and in some cases to 900°C. The investigation also showed that a further...

  18. Cleaning method of the oil field wastewater treatment by UF process

    Institute of Scientific and Technical Information of China (English)

    2001-01-01

    This article introduces experiments and researches of polysulphone ultrafiltration membrane' s effect on oil field polluted water and approaches renewing oil field polluted water and approaches renewing of membrane' s flux by different detergents and cleaning method. Good result has been achieved by doing experiments and the renewal rate of membrane is over 90%.

  19. Estimation of cytogenetic risk among coke oven workers exposed to polycyclic aromatic hydrocarbons.

    Science.gov (United States)

    Sureshkumar, Shanmugam; Balachandar, Vellingiri; Devi, Subramaniam Mohana; Arun, Meyyazhagan; Karthickkumar, Alagamuthu; Balamuralikrishnan, Balasubramanian; Sankar, Kathannan; Mustaqahamed, Shafi Ahammed Khan; Dharwadkar, Shanwaz N; Sasikala, Keshavarao; Cho, Ssang-Goo

    2013-01-01

    Polycyclic aromatic hydrocarbons (PAHs) result from the incomplete combustion of natural or synthetic organic materials. The working environment at a coke plant can negatively affect the employed workers who were exposed to coke oven emissions containing PAHs, which formed and released into the environment by the process of pyrolysis of coke. This study aims to analyze the relationship between the exposure of PAHs and the risk of genetic damages such as chromosomal alteration (CA), micronucleus (MN), and DNA damage (PCR-RFLP) in peripheral blood lymphocytes of 27 coke oven workers and equal number of control subjects. The exposed subjects and controls were divided into two groups based on their age (group Icoke oven workers under risk should be monitored for adverse effects of the any long-term exposure. PMID:24040626

  20. Morphological classification of coke formed from the Castilla and Jazmin crude oils

    International Nuclear Information System (INIS)

    A morphological classification of cokes from the Castilla and Jazmin Colombian crude oils was completed. These heavy-nature crude oils, after being fractioned during the refining stages, were physicochemical characterized and submitted to the coking process. The conclusions of this work are based on the characterization of the feedstock chemical composition according to the type of aromatic carbon. UV visible spectrophotometry and the corresponding micrographs obtained by a Scan Electron Microscope (SEM), in amplification intervals from 100X to 5000X for the samples of formed cokes, were analyzed. Results of this work allowed the determination of the morphological classification intervals in function of the polyaromatic compound concentration ratio (tetraromatic/triaromatic, and diaromatic/triaromatic) of the different coked feedstock. Furthermore, high content of calcium and sulfur in the feedstock promotes morphologies of the associated - shot type

  1. Influence of carbonization conditions on micro-pore structure of foundry formed coke produced with char

    Energy Technology Data Exchange (ETDEWEB)

    Jun Qiao; Jianjun Wu; Jingru Zu; Zhiyuan Gao; Guoli Zhou

    2009-07-01

    There are few studies on coke's micro-pore structure in recent years, however, micro-pore structure of foundry coke determines its macroscopically quality index and reactivity in cupola furnace. Effect of such factors on micro-pore structure were investigated under different carbonization conditions with certain ratio of raw materials and material forming process in this article as charging temperature (A); braised furnace time (B); heating rate of the first stage (C)and the second stage (D) and holding time of ultimate temperature (E). Research showed that charging temperature was the most influential factor on the coke porosity, pore volume, pore size and specific surface area. It is suggested that formation of plastic mass and releasing rate of volatile during carbonization period are two main factors on microstructure of foundry coke while charging temperature contributes most to the above factors. 6 refs., 4 figs., 9 tabs.

  2. Development of low NOx combustion structure in coke oven

    Energy Technology Data Exchange (ETDEWEB)

    Yoshida, S.; Takase, S.; Uchida, M.; Saji, T.; Koyama, H.; Yamamoto, M. [Sumitomo Metal Industry Ltd., Ibaraki (Japan)

    2004-09-01

    One of the targets of the SCOPE21 process was to improve the productivity. To achieve high productivity, the process was applied the following items: (1) ultra super dense brick, (2) thin wall (70 mm), (3) hot coal charging, (4) medium temperature carbonization. As the heat flux for carbonization was needed about 2 times as much as a conventional coke oven, the combustion technologies to achieve high productivity were investigated by using the actual scale combustion test oven. The combustion conditions to achieve low NOx in the waste gas and uniform heating for carbonization were clarified. The coke oven of the pilot plant was designed based on these results. The combustion targets of the low NOx and uniform heating were achieved in the test operation.

  3. 防止炉膛结焦和垮大焦%Prevention of Coking and Off Coking in the Boiler Furnace

    Institute of Scientific and Technical Information of China (English)

    吕哲

    2015-01-01

    This paper mainly describes the main factors affecting the boiler coking, these include coal composition and ash melting point,furnace temperature and the distribution of temperature field, air dynamic field ect.. So, the main measures to prevent coking and off coking in the furnace are control of coking coal into the furnace, improvement of the aerodynamic field in furnace, control of furnace temperature, prevention of the oxygen deficient combustion, the heating surface cleaning, ect..%本文主要叙述了影响锅炉结焦的主要因素包括:原煤成份及灰熔点、炉膛温度及温度场分布、空气动力场等,故防止炉膛结焦和垮大焦的主要措施包括:控制易结焦煤种入炉、改善炉内空气动力场、控制炉膛温度、防止缺氧燃烧、保持受热面清洁等。

  4. Utilization of petrographic analysis for determination of petroleum coke mixtures

    OpenAIRE

    TOPRAK, Selami; SÜTCÜ, Emine CİCİOĞLU; GÜLEN, Fatma Jale

    2014-01-01

    This study was carried out on mostly imported, processed petrocokes, which are also commercially known as "petcoke" or "petroleum coke". Petrocoke is imported in great amounts and is occasionally consumed domestically without conscientious thought. It is not a well-known material, though there is an idea of its genesis. The samples, their analysis, and their images are essential to be kept in mind for further investigations, since it is not an environmental...

  5. Characterization of residual coke during burning

    Energy Technology Data Exchange (ETDEWEB)

    Pieck, C.L.; Jablonski, E.L.; Parera, J.M. (Inst. de Investigaciones in Catalisis y Petroquimica, Santiago del Estero 2654, 3000 Santa Fe (Argentina)); Frety, R. (Conventionne a l' Univ. Claude Bernard, Lyon I (France))

    1992-04-01

    In this paper coke remaining from the partial burning of coke deposited during the commercial re-forming of naphtha on a Pt-Re/Al[sub 2]O[sub 3] catalyst is studied. Burning temperatures are 623-923 K, and the remaining coke is characterized by temperature-programmed oxidation, X-ray diffraction, electron diffraction, IR, [sup 13]C CP-MAS NMR, electron spectroscopy for chemical analysis, electron paramagnetic resonance, and chemical analysis. After coke is burned at 673 K, the residual coke shows the minimum value in the H/C ratio and the maximum in the thickness of the aromatic layers, degree of organization, C==O concentration, binding energy of C 1s, peak width, and g value. This agrees with the model of coke burning: at low temperatures, the burning is selective; the more hydrogenated and amorphous carbonaceous species are burnt first. At high temperatures, the burning is nonselective and all species are simultaneously burnt. Coke is partially oxidized during burning, and intermediate species with C==O and C--OH groups are formed.

  6. Analysis of coal charge drying in a coke oven

    Energy Technology Data Exchange (ETDEWEB)

    Postrzednik, S. (Politechnika Slaska, Gliwice (Poland). Instytut Techniki Cieplnej)

    1987-01-01

    Analyzes drying of coal mixtures charged to a coke oven and factors that influence drying. A mathematical model of coal gasification is used. Coal charge in a coke oven is dried layer by layer starting from the layer adjacent to coke oven walls. Moisture evaporated from a layer close to coke oven walls condenses in a layer more distant from coke oven walls (i.e. in the coke oven center). Formulae that describe moisture migration in a coke oven are derived and formulae that describe coal drying are evaluated. The following factors that influence drying are considered: moisture content in coal, initial coal temperature, condensation temperature, heating wall thickness, coke oven dimensions, final temperature of coking, average temperature in flue channels. Analyses show that 62.8% of coking time falls on drying and condensation. 6 refs.

  7. The New-Generation Technology for Making Petroleum Needle Coke

    Institute of Scientific and Technical Information of China (English)

    Shi Changzhi; Shen Haiping; Long Jun; Xie Changjiang

    2003-01-01

    The current technology for producing the petroleum needle coke is apt to cause overflow of feedstock from the coke drums, instability in operation of coking unit, low mechanical strength of petroleum coke, and high percentage of coke powder, leading to difficulties in improving the overall quality of needle coke. Therefore, we have developed a new technology for producing the needle coke,featuring the manipulation of temperature range in a narrow scale at high pressure coupled with feedstock alternations. This new kind of technology has been successfully applied in a 60kt/a commercial coking unit. Provided that demand for the feedstock quality is satisfied, petroleum needle coke meeting the international quality standard can be manufactured using RIPP's technology for producing petroleum needle coke.

  8. Mechanism of physical transformations of mineral matter in the blast furnace coke with reference to its reactivity and strength

    Energy Technology Data Exchange (ETDEWEB)

    Stanislav S. Gornostayev; Jouko J. Haerkki [University of Oulu, Oulu (Finland). Laboratory of Process Metallurgy

    2006-12-15

    Examinations of polished and dry cut sections of feed and tuyere coke revealed some possible mechanisms for the physical influence of mineral compounds on the reactivity and strength of coke. It was observed that rounded particles of mineral phases that are exposed to the pore walls and surface of coke at high temperature create an inorganic cover, thus reducing the surface available for gas-solid reactions. The particles of mineral matter that have a low melting point and viscosity can affect the coke at earlier stages in the blast furnace process, acting in the upper parts of the blast furnace (BF). The temperature-driven redistribution of mineral phases within the coke matrix probably leads to the creation of weak spots and in general to anisotropy in its properties, thus reducing its strength. 9 refs., 2 figs., 1 tab.

  9. The impact of multiphase behaviour on coke deposition in heavy oil hydroprocessing catalysts

    Science.gov (United States)

    Zhang, Xiaohui

    be proportional to the nominal concentration of coke precursor present in the feed. These new findings are very significant both with respect to providing guidance concerning possible operation improvement for existing processes and for the development of new upgrading processes.

  10. Cancer mortality among coke oven workers.

    OpenAIRE

    Redmond, C K

    1983-01-01

    The OSHA standard for coke oven emissions, which went into effect in January 1977, sets a permissible exposure limit to coke oven emissions of 150 micrograms/m3 benzene-soluble fraction of total particulate matter (BSFTPM). Review of the epidemiologic evidence for the standard indicates an excess relative risk for lung cancer as high as 16-fold in topside coke oven workers with 15 years of exposure or more. There is also evidence for a consistent dose-response relationship in lung cancer mort...

  11. Clean-air legislation will buoy U.S. gas processing

    International Nuclear Information System (INIS)

    This paper reports on the effects of recent U.S. clean-air legislation on NGL demand and pricing. Demand for all NGL products will be firm throughout the 1990s. Increased requirements for butane as methyl tertiary butyl ether (MTBE) feedstock will strengthen butane prices. Higher base-load requirements for propane in new NGL-based olefin plants will also have a positive impact on propane prices

  12. Metal emission into the air from processes of energetic fuel utilization in Poland. Part 2. Burning of brown coal, coke, gas, fuel oil, wood

    International Nuclear Information System (INIS)

    Indicators of metal emission into atmospheric air from burning processes of the above mentioned fuels have been discussed and the emission size of these metals in Poland in 1990 given. (author). 7 refs, 1 fig., 3 tabs

  13. Mortality due to respiratory cancers in the coke oven plants of the Lorraine coalmining industry (Houillères du Bassin de Lorraine).

    OpenAIRE

    Bertrand, J P; Chau, N.; Patris, A.; Mur, J M; Pham, Q T; Moulin, J J; Morviller, P; Auburtin, G; Figueredo, A; Martin, J.

    1987-01-01

    The main activity of the Houillères du Bassin de Lorraine (Lorraine Collieries), employing 23,000 operatives and executives, is coalmining. The coke production is carried out by two coke oven plants with a workforce of respectively 747 and 552 workers. The coal coking process entails the emission of noxious products such as polycyclic aromatic hydrocarbons (PAH) from the ovens. The influence of occupational exposure on mortality due to respiratory cancers, and particularly to lung and upper r...

  14. Clean surface processing of rubrene single crystal immersed in ionic liquid by using frequency modulation atomic force microscopy

    International Nuclear Information System (INIS)

    Surface processing of a rubrene single crystal immersed in ionic liquids is valuable for further development of low voltage transistors operated by an electric double layer. We performed a precise and clean surface processing based on the tip-induced dissolution of rubrene molecules at the ionic liquid/rubrene single crystal interfaces by using frequency modulation atomic force microscopy. Molecular resolution imaging revealed that the tip-induced dissolution proceeded via metastable low density states derived from the anisotropic intermolecular interactions within the crystal structure.

  15. Treatment of coking wastewater by using manganese and magnesium ores

    International Nuclear Information System (INIS)

    This study investigated a wastewater treatment technique based on natural minerals. A two-step process using manganese (Mn) and magnesium (Mg) containing ores were tested to remove typical contaminants from coking wastewater. Under acidic conditions, a reactor packed with Mn ore demonstrated strong oxidizing capability and destroyed volatile phenols, chemical oxygen demand (COD), and sulfide from the coking wastewater. The effluent was further treated by using Mg ore to remove ammonium-nitrogen and phosphate in the form of magnesium ammonium phosphate (struvite) precipitates. When pH of the wastewater was adjusted to 1.2, the removal efficiencies for COD, volatile phenol and sulfide reached 70%, 99% and 100%, respectively. During the second step of precipitation, up to 94% of ammonium was removed from the aqueous phase, and precipitated in the form of struvite with phosphorus. The struvite crystals showed a needle-like structure. X-ray diffraction and transmission electron microscopy were used to characterize the crystallized products.

  16. Parametric Study of Gasification of the Mexican Petroleum Coke: Effect Feed Petroleum Coke on Energetic Characteristic of the Synthetic Gas (syngas

    Directory of Open Access Journals (Sweden)

    Longoria-Ramírez R.

    2011-07-01

    Full Text Available In this work, a parametric study the gasification of the Mexican petroleum coke from the refineries of Cd Madero (CRM and Cadereyta, Nuevo León (CRC is performed. It is evaluates the energy behavior of the gasification process with objective to research which feedstock of petroleum coke has a be?? er yield of energy. Effect feed petroleum coke on energy characteristics of the clear synthetic gas (gasl: molar composition of CO and H2, High Heating Value (HHVgasl, energy power (Ogasl, Cold Gas Efficiency (CGEgasl and thermal efficiency of gasification (?tg is realized. The parametric study has been realized for 0.64 = oxygen/coke = 1.11 ratio with the fl ow of oxygen (6036.388 kg/h and steam/oxygen of 23% both constant. It is observed that in oxygen/coke 0.77 and 0.94 ratio it is present the best energy characteristics of the gasl from CRM and CRC, respectively. The best energy characteristics relationship of the gasl fined are: molar composition CO (65.6, 68.5, H2 (32.29, 29.13, HHVgasl (14054.6 kJ/kggasl, 13438.76 kJ/kggasl, Ogasl (204.86 GJ/h, 178.02 GJ/h, CGEgasl (74.43%, 71.14%, ?tg (86.2%, 83.22%. The gasification of petroleum coke CRM produced energy with 26.20 MJ/kgcoque rates whereas that gasification of the petroleum coke CRC produced 27.74 MJ/kgcoque rates.

  17. Volatiles production from the coking of coal; Sekitan no netsubunkai ni okeru kihatsubun seisei

    Energy Technology Data Exchange (ETDEWEB)

    Yamashita, Y.; Saito, H.; Inaba, A. [National Institute for Resources and Environment, Tsukuba (Japan)

    1996-10-28

    In order to simplify the coke manufacturing process, a coke production mechanism in coal pyrolysis was discussed. Australian bituminous coal which can produce good coke was used for the discussion. At a temperature raising rate of 50{degree}C per minute, coal weight loss increases monotonously. However, in the case of 3{degree}C, the weight loss reaches a peak at a maximum ultimate temperature of about 550{degree}C. The reaction mechanism varies with the temperature raising rates, and in the case of 50{degree}C per minute, volatiles other than CO2 and propane increased. Weight loss of coal at 3{degree}C per minute was caused mainly by methane production at 550{degree}C or lower. When the temperature is raised to 600{degree}C, tar and CO2 increased, and so did the weight loss. Anisotropy was discerned in almost of all coke particles at 450{degree}C, and the anisotropy became remarkable with increase in the maximum ultimate temperature. Coke and volatiles were produced continuously at a temperature raising rate of 50{degree}C per minute, and at 3{degree}C per minute, the production of the coke and volatiles progressed stepwise as the temperature has risen. 7 refs., 6 figs.

  18. Discrete Element Method Modeling of the Rheological Properties of Coke/Pitch Mixtures

    Directory of Open Access Journals (Sweden)

    Behzad Majidi

    2016-05-01

    Full Text Available Rheological properties of pitch and pitch/coke mixtures at temperatures around 150 °C are of great interest for the carbon anode manufacturing process in the aluminum industry. In the present work, a cohesive viscoelastic contact model based on Burger’s model is developed using the discrete element method (DEM on the YADE, the open-source DEM software. A dynamic shear rheometer (DSR is used to measure the viscoelastic properties of pitch at 150 °C. The experimental data obtained is then used to estimate the Burger’s model parameters and calibrate the DEM model. The DSR tests were then simulated by a three-dimensional model. Very good agreement was observed between the experimental data and simulation results. Coke aggregates were modeled by overlapping spheres in the DEM model. Coke/pitch mixtures were numerically created by adding 5, 10, 20, and 30 percent of coke aggregates of the size range of 0.297–0.595 mm (−30 + 50 mesh to pitch. Adding up to 30% of coke aggregates to pitch can increase its complex shear modulus at 60 Hz from 273 Pa to 1557 Pa. Results also showed that adding coke particles increases both storage and loss moduli, while it does not have a meaningful effect on the phase angle of pitch.

  19. Effect of mechanochemical treatment on petroleum coke-CO{sub 2} gasification

    Energy Technology Data Exchange (ETDEWEB)

    Jianhui Zou; Boli Yang; Kaifeng Gong; Shiyong Wu; Zhijie Zhou; Fuchen Wang; Zunhong Yu [East China University of Science and Technology, Shanghai (China). Key Laboratory of Coal Gasification of Ministry of Education

    2008-05-15

    The effect of mechanochemical treatment during the grinding of petroleum coke on its gasification by CO{sub 2} was studied. An additive derived by drying the black liquor in papermaking industry is adopted in grinding process. Results show that the gasification reactivity of petroleum coke is effectively improved by grinding, and the activation by wet grinding is more noticeable than that by dry grinding. Besides, by wet grinding petroleum coke and additive together, the active metal species in additive are not easily volatilized in gasification, and retain a high catalytic reactivity to the coke-CO{sub 2} reaction throughout most of the conversion range. Changes in crystal structure of the petroleum coke induced by mechanochemical treatment is related to its gasification reactivity. In general, the crystalline-amorphous phase transition is the tendency of long time mechanical grinding, while a crystal structure re-formation stage is observed after wet grinding of petroleum coke with and without additive for some time. Similar phenomenon has also been found in the reported data, but not given attention. Some discussion is made in the paper, and more work should be undertaken to disclose the mechanism. 28 refs., 4 figs., 1 tab.

  20. Results of the simulation of gasification of the mexican petroleum coke from the refineries of Ciudad Madero and Cadereyta

    Directory of Open Access Journals (Sweden)

    G. Urquiza–Beltrán

    2008-04-01

    Full Text Available This paper evaluates in terms of energy the gasification of the petroleum coke from the refineries of Cd Madero and Cadereyta in Mexico. The energy evaluation of the synthetic gas (syngas focuses mainly on the chemical composition of the clean syngas (gasl and its energy characteristics: heating value, the energy power, the cold gas efficiency and the thermal efficiency of gasification. The results of the simulation indicate that the gasification of the petroleum coke from Cadereyta called CRC, produces a gasl with better performance and energy characteristics than those obtained when gasifying the coke of petroleum from Cd. Madero, called CRM. When the CRC is gasified, the rate of production of gasl obtained is of 2.07 kggasl/kgcoque, while the rate of production of gasl for the CRM is 1.89 kggasl/kgcoque. The HHV of the gasl of the CRC is 12 729.56 kJ/kggasl while for the CRM is 11 639.13 kJ/kggasl. The energy power of the gasl of the CRC is greater, with a difference of 25.87 GJ/h, with regard to the energy power of the gasl of the CRM. Under the specified conditions of operation, energy is generated ata rate of 26.46 MJ/kgcoque coke in the gasification of the CRC coke of petroleum, while when gasifying the CRM coke of petroleum 22.09 MJ/kgcoque are generated. Currently, the petroleum coke produced in the refinery of Madero is consumed in the power plants of Tamuín, San Luis Potosí, Mexico, while the petroleum coke produced by the refinery of Cadereyta is used in the cement industry.

  1. Formation of coke precursors from pyrene-based model compounds

    Energy Technology Data Exchange (ETDEWEB)

    Alshareef, Ali H.; Gray, Murray R. [Department of Chemical and Materials Engineering, University of Alberta (Canada)], email: murray.gray@ualberta.ca; Azyat, Khalid [Department of Chemistry, University of Alberta (Canada); Tykwinski, Rik [Friedrich-Alexander-Universitat (Germany)

    2010-07-01

    This work highlights understanding the thermal behavior and coking mechanism of pyrene-based model compounds. Microcarbon residue (MCR) was estimated for a thermally cracked model compound (Py-m-Phenyl-Py) using a thermal gravimetric analyzer (TGA). Nevertheless, when the coke produced by this process was analyzed it revealed insignificant information; hence, microreactor experiments were implemented to better analyze residual structures. Py-m-Phenyl-Py was converted with 30% and a mass spectrometry was performed on high molecular weight products, whereas, low molecular cracked weight products were analyzed using GC-MS. It was shown that the products obtained from this process matched those obtained by free-radical cracking. Moreover, MALDI-TOF analysis was used to reveal the addition product, and a spectrum of products was generated. It was shown that most of these products were yielded from the same species. It was believed that cyclization might be characterized by the dehydrogenation of the addition products, and coke precursors were generated due to olefin formation and radical additions.

  2. Human health risk characterization of petroleum coke calcining facility emissions.

    Science.gov (United States)

    Singh, Davinderjit; Johnson, Giffe T; Harbison, Raymond D

    2015-12-01

    Calcining processes including handling and storage of raw petroleum coke may result in Particulate Matter (PM) and gaseous emissions. Concerns have been raised over the potential association between particulate and aerosol pollution and adverse respiratory health effects including decrements in lung function. This risk characterization evaluated the exposure concentrations of ambient air pollutants including PM10 and gaseous pollutants from a petroleum coke calciner facility. The ambient air pollutant levels were collected through monitors installed at multiple locations in the vicinity of the facility. The measured and modeled particulate levels in ambient air from the calciner facility were compared to standards protective of public health. The results indicated that exposure levels were, on occasions at sites farther from the facility, higher than the public health limit of 150 μg/m(3) 24-h average for PM10. However, the carbon fraction demonstrated that the contribution from the calciner facility was de minimis. Exposure levels of the modeled SO2, CO, NOx and PM10 concentrations were also below public health air quality standards. These results demonstrate that emissions from calcining processes involving petroleum coke, at facilities that are well controlled, are below regulatory standards and are not expected to produce a public health risk. PMID:26520182

  3. Plasma Cleaning

    Science.gov (United States)

    Hintze, Paul E.

    2016-01-01

    NASA's Kennedy Space Center has developed two solvent-free precision cleaning techniques: plasma cleaning and supercritical carbon dioxide (SCCO2), that has equal performance, cost parity, and no environmental liability, as compared to existing solvent cleaning methods.

  4. A novel process for preparation of ultra-clean micronized coal by high pressure water jet comminution technique

    Energy Technology Data Exchange (ETDEWEB)

    Longlian Cui; Liqian An; Weili Gong; Hejin Jiang [China University of Mining and Technology, Beijing (China). School of Mechanics, Architecture and Civil Engineering

    2007-03-15

    A novel process for the preparation of ultra-clean micronized coal is presented in this paper. High pressure water jet mill replacing the ball mill is employed for coal comminution in the new preparation process, which is the essential difference from the traditional one. To compare the new preparation process with the traditional one, the comparison experiments were performed, with froth flotation tests of the fine particles ground by both mills using diesel oil and n-dodecane as collector, 2-octanol as frother, and sink-float separation tests using mixtures of carbon tetrachloride-benzene and carbon tetrachloride-bromoform as dense liquid. Different parameters including combustible recovery, ash content of the clean coal, separation efficiency, and energy consumption were investigated based on the two different preparation processes. The results show that the new preparation process has high combustible recovery, low ash content of the product, high separation efficiency, and low energy consumption compared with the traditional one. The comminution mechanism of high pressure water jet mill is introduced in this paper. The high pressure water jet comminution technique has great potential in coal pulverization, having the advantages of low energy consumption, low iron content, and low equipment wear. 35 refs., 4 figs., 7 tabs.

  5. Coke oven automatic combustion control system

    Energy Technology Data Exchange (ETDEWEB)

    Shihara, Y.

    1981-01-01

    This article describes and discusses the development and application of an automatic combustion control system for coke ovens that has been used at the Yawata Works of the Nippon Steel Corporation, Japan. (In Japanese)

  6. Economics and alternatives for sulfur removal from coke oven gas

    Energy Technology Data Exchange (ETDEWEB)

    Massey, M.J.; Dunlap, R.W.

    1975-10-01

    Two processes are currently being employed in North America for the desulfurization of coke oven gas, the Vacuum Carbonate System, and the Stretford System. A third, the Sulfiban Process, which was recently announced, now has several plants scheduled for construction. Overall operating requirements for each of these processes are considered in detail. Emphasis is placed on an identification of power and steam requirements, the types and amounts of solid and/or liquid waste streams produced together with methods for their treatment, and the net desulfurization efficiencies achieved by each process. Detailed estimates of capital and operating costs for desulfurization are considered, and equipment needs for environmental control requirements are discussed.

  7. Method of determining coking temperature of coke. [Experimental method of determining final coking temperature using a small sample and calibration graph

    Energy Technology Data Exchange (ETDEWEB)

    Mel' nichuk, A.Yu.; Bondarenko, A.K.; Fialkov, B.S.; Khegay, L.U.; Khvan, L.A.; Muzyzhuk, V.D.; Zakharov, A.G.; Zelenskiy, V.P.

    1985-01-01

    The coking temperature of coke should be determined from the magnitude of the ionization current of the medium during heating (3/sup 0//min) of a coke sample (2 g, fraction < 0.2 mm) in an oxidation medium with air supply (1 1/min). The coking temperature is determined from the maximum magnitude of current using a graduated graph constructed during analysis of coke samples obtained with different final coking temperatures. The discrepancy between the established coking temperature and that defined from the proposed method is 8-19/sup 0/, and that defined from electrical resistance of coke is 26-43/sup 0/. In addition to high accuracy, this method reduces the time outlays for making the analysis.

  8. Modelling of a coke oven heating wall

    OpenAIRE

    Landreau, M.; Isler, D.; Gasser, A.; Blond, E.; Daniel, J.-L.

    2011-01-01

    International audience This work deals with thermomechanical modelling of a coke oven heating wall. The objective is to define the safe limits of coke oven battery operating conditions compatible with a long service life in terms of thermal and mechanical stresses. For this purpose a 3D thermomechanical model of a heating wall taking into account the assembly of bricks and joints was developed with PRISME Laboratory. To build an efficient and complete model, different parameters must be ta...

  9. Study of coke oven combustion control

    Energy Technology Data Exchange (ETDEWEB)

    Nakagawa, F.; Ono, H.; Ariyoshi, K.; Kasaoka, H.; Ichinomiya, M.

    1986-01-01

    Gas flow and combustion in the flues of a Carl Still-type coke oven battery (employing natural draft) can be controlled by focussing on combustion control for a single oven and applying an equation for steady gas flow to all the gas passages in the combustion chambers. This effectively corrects the oven temperature distribution. The usefulness of this control technique has been confirmed, and a large reduction in coking heat consumption has been achieved. 1 ref., 3 figs.

  10. Process Optimization of Ammonia Steam Heating System in Coking Plant%焦化厂蒸氨供热系统工艺优化

    Institute of Scientific and Technical Information of China (English)

    苏琼

    2015-01-01

    主要阐述了焦化厂蒸氨塔供热系统工艺优化方案,介绍了蒸汽喷射热泵在蒸氨系统中的应用。运行结果证明,蒸氨塔供热系统工艺优化后取得了良好的节能降耗效果。%The process optimization of ammonia distil ation tower heating system is elaborated.And the application of steam injection hot pump in ammonia steam system is introduced.The running results show that good energy saving effect is achieved after the optimization of ammonia distil ation tower heating system.

  11. Identification of causes of oil sands coke leachate toxicity

    Energy Technology Data Exchange (ETDEWEB)

    Puttaswamy, N.; Liber, K. [Saskatchewan Univ., Regina, SK (Canada)

    2010-07-01

    The potential causes of oil sands coke leachate toxicity were investigated. Chronic 7-day toxicity tests were conducted to demonstrate that oil sands coke leachates (CL) are acutely toxic to Ceriodaphnia dubia (C. dubia). CLs were generated in a laboratory to perform toxicity identification evaluation (TIE) tests in order to investigate the causes of the CL toxicity. The coke was subjected to a 15-day batch leaching process at 5.5 and 9.5 pH values. The leachates were then filtered and used for chemical and toxicological characterization. The 7-day estimates for the C. dubia survival were 6.3 for a pH of 5.5 and 28.7 per cent for the 9.5 CLs. The addition of EDTA significantly improved survival and reproduction in a pH of 5.5 CL, but not in a pH of 9.5 CL. The toxicity of the pH 5.5 CL was removed with a cationic resin treatment. The toxicity of the 9.5 pH LC was removed using an anion resin treatment. Toxicity re-appeared when nickel (Ni) and vanadium (V) were added back to the resin-treated CLs. Results of the study suggested that Ni and V were acting as primary toxicants in the pH 5.5 CL, while V was the primary cause of toxicity in the pH 9.5 CL.

  12. Identification of causes of oil sands coke leachate toxicity

    International Nuclear Information System (INIS)

    The potential causes of oil sands coke leachate toxicity were investigated. Chronic 7-day toxicity tests were conducted to demonstrate that oil sands coke leachates (CL) are acutely toxic to Ceriodaphnia dubia (C. dubia). CLs were generated in a laboratory to perform toxicity identification evaluation (TIE) tests in order to investigate the causes of the CL toxicity. The coke was subjected to a 15-day batch leaching process at 5.5 and 9.5 pH values. The leachates were then filtered and used for chemical and toxicological characterization. The 7-day estimates for the C. dubia survival were 6.3 for a pH of 5.5 and 28.7 per cent for the 9.5 CLs. The addition of EDTA significantly improved survival and reproduction in a pH of 5.5 CL, but not in a pH of 9.5 CL. The toxicity of the pH 5.5 CL was removed with a cationic resin treatment. The toxicity of the 9.5 pH LC was removed using an anion resin treatment. Toxicity re-appeared when nickel (Ni) and vanadium (V) were added back to the resin-treated CLs. Results of the study suggested that Ni and V were acting as primary toxicants in the pH 5.5 CL, while V was the primary cause of toxicity in the pH 9.5 CL.

  13. Development and application of a new software tool for the basic design of flue gas cleaning processes

    Energy Technology Data Exchange (ETDEWEB)

    Schausberger, P.; Friedl, A. [Vienna Univ. of Technology, Inst. of Chemical Engineering, Group of Thermal Process Engineering and Simulation, Vienna (Austria); Wieland, A.; Reissner, H. [AE and E Austrian Energy and Environment AG, Flue Gas Cleaning Div., Raaba/Graz (Austria)

    2004-07-01

    The development of a new software tool designed for improvement of the basic engineering of flue-gas cleaning processes and its specific application is presented. The tool is based on the commercially available simulation tool IPSEpro originating from the field of power engineering. Here, a modelling environment enables the enhancement of the existing content: substances, streams and unit operations to be included are structured in an object-oriented manner, the according steady mass and heat balances are setup to yield a system of equations to be solved simultaneously. (orig.)

  14. Hybrid Pressure Retarded Osmosis−Membrane Distillation (PRO−MD) Process for Osmotic Power and Clean Water Generation

    KAUST Repository

    Han, Gang

    2015-05-20

    A novel pressure retarded osmosis−membrane distillation (PRO−MD) hybrid process has been experimentally conceived for sustainable production of renewable osmotic power and clean water from various waters. The proposed PRO−MD system may possess unique advantages of high water recovery rate, huge osmotic power generation, well controlled membrane fouling, and minimal environmental impacts. Experimental results show that the PRO−MD hybrid process is promising that not only can harvest osmotic energy from freshwater but also from wastewater. When employing a 2 M NaCl MD concentrate as the draw solution, ultrahigh power densities of 31.0 W/m2 and 9.3 W/m2 have been demonstrated by the PRO subsystem using deionized water and real wastewater brine as the feeds, respectively. Simultaneously, high purity potable water with a flux of 32.5−63.1 L/(m2.h) can be produced by the MD subsystem at 40−60 °C without any detrimental effects of fouling. The energy consumption in the MD subsystem might be further reduced by applying a heat exchanger in the hybrid system and using low-grade heat or solar energy to heat up the feed solution. The newly developed PRO−MD hybrid process would provide insightful guidelines for the exploration of alternative green technologies for renewable osmotic energy and clean water production.

  15. Coal and coke - Analysis and testing - Coal and coke - Chlorine - High-temperature combustion method

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    2003-09-29

    This Standard sets out a method for the liberation of the chlorine from coal and coke by high-temperature combustion, and its subsequent determination by titrimetry. The presence of residual halogen-bearing organic float-and-sink liquids in coal samples will affect the determination of chlorine. This Standard is applicable to coal and coke containing less than 0.3% chlorine.

  16. Combustion characteristics of coke oven. Developments of combustion control for coke oven - I

    Energy Technology Data Exchange (ETDEWEB)

    Tamura, Y.

    1984-01-01

    This short article is a synopsis of a paper presented to the 106th Meeting of the ISIJ in October 1983. It reports the results of an investigation which showed the effect of flue temperature distribution on coke strength. The results indicate the necessity for controlling the flue top temperature for a single-stage burner coke oven such as the Koppers type.

  17. Torrefaction reduction of coke formation on catalysts used in esterification and cracking of biofuels from pyrolysed lignocellulosic feedstocks

    Energy Technology Data Exchange (ETDEWEB)

    Kastner, James R; Mani, Sudhagar; Hilten, Roger; Das, Keshav C

    2015-11-04

    A bio-oil production process involving torrefaction pretreatment, catalytic esterification, pyrolysis, and secondary catalytic processing significantly reduces yields of reactor char, catalyst coke, and catalyst tar relative to the best-case conditions using non-torrefied feedstock. The reduction in coke as a result of torrefaction was 28.5% relative to the respective control for slow pyrolysis bio-oil upgrading. In fast pyrolysis bio-oil processing, the greatest reduction in coke was 34.9%. Torrefaction at 275.degree. C. reduced levels of acid products including acetic acid and formic acid in the bio-oil, which reduced catalyst coking and increased catalyst effectiveness and aromatic hydrocarbon yields in the upgraded oils. The process of bio-oil generation further comprises a catalytic esterification of acids and aldehydes to generate such as ethyl levulinate from lignified biomass feedstock.

  18. Automatic combustion control in coke oven plants; Controle automatico de combustao em baterias de coque

    Energy Technology Data Exchange (ETDEWEB)

    Torres, Afonso E.; Bissoli, Aluizio R.; Clemente, Jose M.; Oliveira, Jorge M. de; Alves, Marcelo T.; Silva, Mauro R. da [Companhia Siderurgica de Tubarao (CST), Serra, ES (Brazil)

    1996-12-31

    The Automatic Combustion Control of the three Coke Ovens Plants of CST had its first stage started in january 1996, when the Visual Inspection of the Coking End Point was replaced by the Automatic Detection with a Process Computer and thermocouples in the ascension pipes of the 147 ovens. Monitoring is performed in the operations of charging, leveling, discharging, guiding and moving of the 12 movable machines (charging car, discharging car, guide car and locomotive), and safe integrated functioning among these machines is done, using one Plc in each one. The data from each oven are transmitted to the Process Computer by radio waves. Based on temperatures reached by thermocouples installed in the combustion chambers of 10 walls in each coke oven plant, and the automatic detection of weight and moisture of the coal, the Process Computer performs the calculation of the Set Point of the temperature for each coke oven plant. The mathematical model in the Process Computer is responsible for this result and the value is sent to the Plc, in the operation room, in order to control the rate of combustible gas, The cooking time is controlled by this method and the results of coke production are in the target range. (author) 9 figs., 3 tabs.

  19. Solidification of liquid waste from the Freon based dry cleaning process

    International Nuclear Information System (INIS)

    The operating license of the BNPD-S radioactive waste management facility does not permit the storage of radioactive liquids. Samples of Freon based waste have been analyzed and two solidification methods for these samples were investigated in this work. Waste from the commissioning of the dry cleaning facility contains in excess of 96% Freon 113 and it is recommended that this waste be redistilled to recover the Freon. The preferred immobilization technique involves absorption of the waste into a porous medium. This should be adequate for storage purposes. When disposal facilities are available and if the activity of the waste is measurable then the mixture together with its container can be encapsulated in cement. Incineration of the waste is expected to produce corrosive gases as a result of the thermal decomposition of Freon 113 and is not recommended unless the Freon content can be substantially reduced

  20. Black silicon with self-cleaning surface prepared by wetting processes.

    Science.gov (United States)

    Zhang, Ting; Zhang, Peng; Li, Shibin; Li, Wei; Wu, Zhiming; Jiang, Yadong

    2013-01-01

    This paper reports on a simple method to prepare a hydrophobic surface on black silicon, which is fabricated by metal-assisted wet etching. To increase the reaction rate, the reaction device was placed in a heat collection-constant temperature type magnetic stirrer and set at room temperature. It was demonstrated that the micro- and nanoscale spikes on the black silicon made the surface become hydrophobic. As the reaction rate increases, the surface hydrophobicity becomes more outstanding and presents self-cleaning until the very end. The reflectance of the black silicon is drastically suppressed over a broad spectral range due to the unique geometry, which is effective for the enhancement of absorption. PMID:23941184

  1. Steam generators secondary side chemical cleaning at Point Lepreau using the Siemens high temperature process

    Energy Technology Data Exchange (ETDEWEB)

    Verma, K.; MacNeil, C. [New Brunswick Power Corp., Lepreau (Canada); Odar, S.; Kuhnke, K. [Siemens AG, Erlangen (Germany)

    1997-02-01

    This paper describes the chemical cleaning of the four steam generators at the Point Lepreau facility, which was accomplished as a part of a normal service outage. The steam generators had been in service for twelve years. Sludge samples showed the main elements were Fe, P and Na, with minor amounts of Ca, Mg, Mn, Cr, Zn, Cl, Cu, Ni, Ti, Si, and Pb, 90% in the form of Magnetite, substantial phosphate, and trace amounts of silicates. The steam generators were experiencing partial blockage of broached holes in the TSPs, and corrosion on tube ODs in the form of pitting and wastage. In addition heat transfer was clearly deteriorating. More than 1000 kg of magnetite and 124 kg of salts were removed from the four steam generators.

  2. State-of-the-Art Evaluation of Ultra-Clean ULSI Processes^*

    Science.gov (United States)

    Fischer-Colbrie, Alice M.

    1996-03-01

    Ultra-clean Si wafer surfaces are critical to the fabrication of ULSI-quality gate oxides. At present, the best methods for removing surface metal impurities exceeds our ability to measure them using traditional methods. New methods are being actively developed to fill this gap. One approach has been to extend the capability of a technique widely used throughout the semiconductor industry, total reflection x-ray fluorescence (TXRF), by using synchrotron radiation. To date, synchrotron radiation total reflection x-ray fluorescence (SR TXRF) has a state-of-the-art transition metal sensitivity of ~ 3 × 10^8/cm^2 (AMD; D. Werho, Motorola, Inc.; M. Zaitz, IBM; J. Rose, DEC; L. Files, Texas Instruments; K. Gupta, Intel; Synchrotron radiation experiments were performed at the Stanford Synchrotron Radiation Laboratory which is funded by the Department of Energy, Office of Basic Energy Sciences.

  3. CPICOR{trademark}: Clean power from integrated coal-ore reduction

    Energy Technology Data Exchange (ETDEWEB)

    Wintrell, R.; Miller, R.N.; Harbison, E.J.; LeFevre, M.O.; England, K.S.

    1997-12-31

    The US steel industry, in order to maintain its basic iron production, is thus moving to lower coke requirements and to the cokeless or direct production of iron. The US Department of Energy (DOE), in its Clean Coal Technology programs, has encouraged the move to new coal-based technology. The steel industry, in its search for alternative direct iron processes, has been limited to a single process, COREX{reg_sign}. The COREX{reg_sign} process, though offering commercial and environmental acceptance, produces a copious volume of offgas which must be effectively utilized to ensure an economical process. This volume, which normally exceeds the internal needs of a single steel company, offers a highly acceptable fuel for power generation. The utility companies seeking to offset future natural gas cost increases are interested in this clean fuel. The COREX{reg_sign} smelting process, when integrated with a combined cycle power generation facility (CCPG) and a cryogenic air separation unit (ASU), is an outstanding example of a new generation of environmentally compatible and highly energy efficient Clean Coal Technologies. This combination of highly integrated electric power and hot metal coproduction, has been designated CPICOR{trademark}, Clean Power from Integrated Coal/Ore Reduction.

  4. 连杆高压喷淋清洗工艺的设计%The Design of High Pressure Spray Cleaning Process of Connecting Rod

    Institute of Scientific and Technical Information of China (English)

    邓建胜

    2014-01-01

    Combined with an enterprise connecting rod cleaning process, based on connecting rod this general process of cleaning technology, Research high pressure water jet cleaning technology and drying technology, making analysis and comparison , determine the shape of nozzle and mechanism of cleaning.%在当前连杆清洗技术一般工艺流程的基础上,结合某企业连杆清洗的工艺过程,研究了高压喷射清洗技术及干燥技术,做出分析比较及确定喷嘴形状和最终的清洗机理。

  5. Conversion of unrefined coke oven gas by partial pulse combustion

    Energy Technology Data Exchange (ETDEWEB)

    Wuennenberg, W.; George, D.; Habermehl, D.; Rohde, W.

    1984-05-10

    To convert coke-oven gas to a chemical feedstock it is possible to use pulsating partial-oxidation in a pulse tube, a method which yields a hydrogen- and CO-based gas which can serve as a synthesis gas, for example in methanol synthesis. Alternatively, the pulse-tube gas can also be used as a reducer gas in the metallurgical industry. A particular process-related advantage of such a pulse-tube reactor, the so-called Schmid tube, lies in the fact that it gives about a tenfold higher space-time yield than the conventional partial-oxidation process.

  6. KRESS INDIRECT DRY COOLING SYSTEM, BETHLEHEM STEEL'S COKE PLANT DEMONSTRATION AT SPARROWS POINT, MARYLAND - VOLUME 1. TECHNICAL REPORT AND APPENDICES A-F

    Science.gov (United States)

    The report evaluates the Kress Indirect Dry Cooling (KIDC) process, an innovative system for handling and cooling coke produced from a slot-type by-product coke oven battery. he report is based on the test work and demonstration of the system at Bethlehem Steel Corporation's Spar...

  7. Rare regions and Griffiths singularities at a clean critical point: the five-dimensional disordered contact process.

    Science.gov (United States)

    Vojta, Thomas; Igo, John; Hoyos, José A

    2014-07-01

    We investigate the nonequilibrium phase transition of the disordered contact process in five space dimensions by means of optimal fluctuation theory and Monte Carlo simulations. We find that the critical behavior is of mean-field type, i.e., identical to that of the clean five-dimensional contact process. It is accompanied by off-critical power-law Griffiths singularities whose dynamical exponent z' saturates at a finite value as the transition is approached. These findings resolve the apparent contradiction between the Harris criterion, which implies that weak disorder is renormalization-group irrelevant, and the rare-region classification, which predicts unconventional behavior. We confirm and illustrate our theory by large-scale Monte Carlo simulations of systems with up to 70(5) sites. We also relate our results to a recently established general relation between the Harris criterion and Griffiths singularities [Phys. Rev. Lett. 112, 075702 (2014)], and we discuss implications for other phase transitions. PMID:25122283

  8. Influence of properties of bituminous binders on the strength of formed coke

    Energy Technology Data Exchange (ETDEWEB)

    Sharma, Ashok K.; Das, Bani P.; Tripathi, Prem S.M. [Central Fuel Research Institute, P.O. FRI-828108, Dhanbad (India)

    2002-03-20

    The role of different chemical characteristics (coking value, quinoline insolubles, elemental composition, {beta}-resin, toluene solubles) of various coal tar- and petroleum-based bituminous binders, such as heavy fraction of HTC tar, processed LTC tar, pitch and asphalt as also the mixed binder in controlling the strength of formed coke made from char prepared from non-coking Chirimiri coal and coke breeze (prepared after carbonising Jharia coal), respectively, has been studied in some detail. The objective was to investigate as to whether and how the properties of these bituminous binders govern the strength of formed coke. It is found that these properties of the binders do play significantly important role in controlling the strength of formed coke both during curing and carbonisation. These parameters of the binders are found to be closely related with their atomic C/H ratios. Notwithstanding the varying composition of the binders of different origin, be they coal tar or petroleum based, the atomic C/H ratio seems to be the most important characteristics of the bituminous binders, upon which the strength of formed coke depends predominantly. This also holds true when mixed binders were used. The results show that at a C/H ratio of about 1, the strength of the briquettes either on curing or on carbonising remains almost similar and that strong cured briquettes can be produced by using a bituminous binder with a C/H ratio less than 1, whilst for obtaining strong carbonised briquettes, binders with C/H ratio greater than 1 are preferable.

  9. Is dry cleaning all wet?

    International Nuclear Information System (INIS)

    Chemical solvents from dry cleaning, particularly perchloroethylene (perc), have contributed to groundwater contamination, significant levels of air pollution in and around cleaners, and chemical accumulation in food. Questions are being raised about the process of cleaning clothes with chemical, and other less toxic cleaning methods are being explored. The EPA has focused attention on the 50 year old Friedburg method of cleaning, Ecoclean, which uses no dangerous chemicals and achieves comparable results. Unfortunately, the cleaning industry is resistant to change, so cutting back on amount of clothes that need dry cleaning and making sure labels aren't exaggerating when they say dry clean only, is frequently the only consumer option now

  10. Gas Chromatography Method of Cleaning Validation Process for 2-Propanol Residue Determination in Pharmaceutical Manufacturing Equipment

    Directory of Open Access Journals (Sweden)

    Łukasz Czubak

    2014-07-01

    Full Text Available Cleaning validation is an integral operation of good manufacturing practice in pharmaceutical industry. The aim of this study was to validate simple analytical method for detection of 2-propanol residue in equipment, which is likely contaminated with 2-propanol, usually used in the production area. The gas chromatography with flame ionization detection (GC-FID method was validated on a GC system using DB-FFAP capillary column at the flow rate of 4.9 mL/min. The calibration curve was linear over concentration range from 2.8µg/mL to 110.7µg/mL with a correlation coefficient equal to 0.99981. The detection limit (LOD and quantitation limit (LOQ were 1.1µg/mL and 2.8µg/mL, respectively. The simplicity of gas chromatography method makes it useful for routine analysis of 2-propanol residue and is an alternative to corresponding methods.

  11. METALLURGICAL COKE INDUSTRY PARTICULATE EMISSIONS: SOURCE CATEGORY REPORT

    Science.gov (United States)

    The report gives results of a study to develop particulate emission factors based on cutoff size for inhalable particles for the metallurgical coke industry. After a review of available information characterizing particulate emissions from metallurgical coke plants, the data were...

  12. Study and modelling of deactivation by coke in catalytic reforming of hydrocarbons on Pt-Sn/Al{sub 2}O{sub 3} catalyst; La microbalance inertielle: etude et modelisation cinetique de la desactivation par le coke en reformage catalytique des hydrocarbures sur catalyseur Pt-Sn/Al{sub 2}O{sub 3}

    Energy Technology Data Exchange (ETDEWEB)

    Mathieu-Deghais, S.

    2004-07-01

    Catalytic reforming is the refining process that produces gasoline with a high octane number. During a reforming operation, undesired side reactions promote the formation of carbon deposits (coke) on the surface of the catalyst. As the reactions proceed, the coke accumulation leads to a progressive decrease of the catalyst activity and to a change in its selectivity. Getting this phenomenon under control is interesting to optimize the industrial plants. This work aims to improve the comprehension and the modeling of coke formation and its deactivating effect on reforming reactions, while working under conditions chosen within a range as close as possible to the industrial conditions of the regenerative process. The experimental study is carried out with a micro unit that is designed to observe simultaneously the coke formation and its influence on the catalyst activity. A vibrational microbalance reactor (TEOM - Tapered Element Oscillating Microbalance) is used to provide continuous monitoring of coke. On-line gas chromatography is used to observe the catalyst activity and selectivity as a function of the coke content. The coking experiments are performed on a fresh Pt-Sn/alumina catalyst, with mixtures of hydrocarbon molecules of 7 carbon atoms as hydrocarbon feeds. The coking tests permitted to highlight the operating parameters that may affect the amount of coke, and to identify the hydrocarbon molecules that behave as coke intermediate. A kinetic model for coke formation could be developed through the compilation of these results. The catalytic activity analysis permitted to point out the coke effect on both of the active phases of the catalyst, to construct a simplified reforming kinetic model that simulates the catalyst activity under the reforming conditions, and to quantify deactivation via deactivation functions. (author)

  13. Fissure formation in coke. 3: Coke size distribution and statistical analysis

    Energy Technology Data Exchange (ETDEWEB)

    D.R. Jenkins; D.E. Shaw; M.R. Mahoney [CSIRO, North Ryde, NSW (Australia). Mathematical and Information Sciences

    2010-07-15

    A model of coke stabilization, based on a fundamental model of fissuring during carbonisation is used to demonstrate the applicability of the fissuring model to actual coke size distributions. The results indicate that the degree of stabilization is important in determining the size distribution. A modified form of the Weibull distribution is shown to provide a better representation of the whole coke size distribution compared to the Rosin-Rammler distribution, which is generally only fitted to the lump coke. A statistical analysis of a large number of experiments in a pilot scale coke oven shows reasonably good prediction of the coke mean size, based on parameters related to blend rank, amount of low rank coal, fluidity and ash. However, the prediction of measures of the spread of the size distribution is more problematic. The fissuring model, the size distribution representation and the statistical analysis together provide a comprehensive capability for understanding and predicting the mean size and distribution of coke lumps produced during carbonisation. 12 refs., 16 figs., 4 tabs.

  14. 生物质焦油催化裂解过程中酸性催化剂积碳失活与烧焦再生特性%Deactivation and Burning Regeneration of Coked Acid Catalysts in Catalytic Cracking Process of Biomass Tar

    Institute of Scientific and Technical Information of China (English)

    李永玲; 吴占松

    2014-01-01

    为了研究酸性催化剂积碳失活以及再生特性,在固定床反应器上,以高铝砖作为催化剂,进行了生物质焦油催化裂解实验。实验结果表明,由于催化剂表面积碳,造成催化剂活性随着作用时间增加而下降。但当催化剂工作一定时间后,催化剂表面的积碳速率开始变得平缓,单层积碳向多层积碳转变。当积碳速率与反应中焦炭脱除速率达到平衡时,催化剂表面积碳量将趋于稳定。实验中采用烧焦法有效地恢复了催化剂的活性,但是焦炭燃烧会破坏催化剂表面的酸性结构,减少表面活化位,使得再生后的催化剂并不能完全达到新鲜催化剂所具有的催化能力。而且烧焦再生过程中会发生烧结,结晶等现象,改变催化剂的孔隙率、孔径分布、比表面积等物理特性。%In order to study the activity regeneration of deactivating acid catalysts with carbon deposition, the catalytic cracking experiments on biomass tar were carried out in a fixed bed reactor with high-alumina brick as acid catalyst. The results show that the catalyst activity declines with the increase of reaction time, due to the carbon depositing on catalyst surface. The carbon depositing rate on catalyst surface becomes smooth after a period of work time, and the mode of coke deposition becomes multi-layer form monolayer. The quantities of the carbon depositing on the catalyst surface will be stable, when the coking rate is equal to the rate of coke consumption. The regeneration method of coke burning can effectively recover the activity of catalyst. But the activity of regenerated catalyst cannot be the same as that of fresh catalyst, because the acidic structure and active center on catalyst surface are destroyed in coke combustion process. In addition, the sintering or crystallization phenomenon will occur in catalysts regeneration process with coke burning, which may change the physical

  15. Model Predictive Control with Feedforward Strategy for Gas Collectors of Coke Ovens

    Institute of Scientific and Technical Information of China (English)

    Kai Li; Dewei Li; Yugeng Xi; Debin Yin

    2014-01-01

    In coking process, the production quality, equipment life, energy consumption, and process safety are all influenced by the pressure in gas collector pipe of coke oven, which is frequently influenced by disturbances. The main control objectives for the gas collector pressure system are keeping the pressures in collector pipes at appropriate operating point. In this paper, model predictive control (MPC) strategy is introduced to control the collector pressure system due to its ability to handle constraint and good control performance. Based on a method proposed to simplify the system model, an extended state space model predictive control is designed, which combines the feedforward strategy to eliminate the disturbance. The simulation results in a system with two coke ovens show the feasibility and effectiveness of the control scheme.

  16. TREATMENT TANK OFF-GAS TESTING FOR THE ENHANCED CHEMICAL CLEANING PROCESS

    Energy Technology Data Exchange (ETDEWEB)

    Wiersma, B.

    2011-08-29

    The purpose of this activity was to provide a bounding estimate of the volume of hydrogen gas generated during Enhanced Chemical Cleaning (ECC) of residual sludge remaining in a Type I or Type II treatment tank as well as to provide results independent of the sludge volume in the waste tank to be cleaned. Previous testing to support Chemical Cleaning was based on a 20:1 oxalic acid to sludge ratio. Hydrogen gas evolution is the primary safety concern. Sealed vessel coupon tests were performed to estimate the hydrogen generation rate due to corrosion of carbon steel by 2.5 wt.% oxalic acid. These tests determined the maximum instantaneous hydrogen generation rate, the rate at which the generation rate decays, and the total hydrogen generated. These values were quantified based on a small scale methodology similar to the one described in WSRC-STI-2007-00209, Rev. 0. The measured rates support identified Safety Class functions. The tests were performed with ASTM A285 Grade C carbon steel coupons. Bounding conditions were determined for the solution environment. The oxalic acid concentration was 2.5 wt.% and the test temperature was 75 C. The test solution was agitated and contained no sludge simulant. Duplicate tests were performed and showed excellent reproducibility for the hydrogen generation rate and total hydrogen generated. The results showed that the hydrogen generation rate was initially high, but decayed rapidly within a couple of days. A statistical model was developed to predict the instantaneous hydrogen generation rate as a function of exposure time by combining both sets of data. An upper bound on the maximum hydrogen generation rate was determined from the upper 95% confidence limit. The upper bound confidence limit for the hydrogen generation rate is represented by the following equation. ln (G{sub v}) = -8.22-0.0584 t + 0.0002 t{sup 2}. This equation should be utilized to estimate the instantaneous hydrogen generation rate per unit surface area, G

  17. 29 CFR 1910.1029 - Coke oven emissions.

    Science.gov (United States)

    2010-07-01

    ... 29 Labor 6 2010-07-01 2010-07-01 false Coke oven emissions. 1910.1029 Section 1910.1029 Labor... Coke oven emissions. (a) Scope and application. This section applies to the control of employee exposure to coke oven emissions, except that this section shall not apply to working conditions with...

  18. Development of coke oven combustion control technology (II): analysis of coke oven operation

    Energy Technology Data Exchange (ETDEWEB)

    Tamura, Y.; Yamamura, H.; Yamamoto, T.; Katayama, A.; Takase, S.

    1983-01-01

    Following on from an earlier report continuous measurements were carried out in an operating oven to establish when coking in the upper coke oven chamber was completed. The results of this operational analysis are reported. Accounts are also given of the measures adopted, on the basis of these results, to reduce the variations in coke quality. These measures, which constitute a combustion control system, include using a carbonization model to calculate the correct temperature distribution and then adjusting the burner ports accordingly. 1 reference.

  19. Automated cleaning of electronic components

    International Nuclear Information System (INIS)

    Environmental and operator safety concerns are leading to the elimination of trichloroethylene and chlorofluorocarbon solvents in cleaning processes that remove rosin flux, organic and inorganic contamination, and particulates from electronic components. Present processes depend heavily on these solvents for manual spray cleaning of small components and subassemblies. Use of alternative solvent systems can lead to longer processing times and reduced quality. Automated spray cleaning can improve the quality of the cleaning process, thus enabling the productive use of environmentally conscious materials, while minimizing personnel exposure to hazardous materials. We describe the development of a prototype robotic system for cleaning electronic components in a spray cleaning workcell. An important feature of the prototype system is the capability to generate the robot paths and motions automatically from the CAD models of the part to be cleaned, and to embed cleaning process knowledge into the automatically programmed operations

  20. Clean data

    CERN Document Server

    Squire, Megan

    2015-01-01

    If you are a data scientist of any level, beginners included, and interested in cleaning up your data, this is the book for you! Experience with Python or PHP is assumed, but no previous knowledge of data cleaning is needed.

  1. Influence of biomass on metallurgical coke quality

    OpenAIRE

    Montiano Redondo, María de Garabandal; Díaz-Faes González, Elvira; Barriocanal Rueda, Carmen; Álvarez García, Ramón

    2014-01-01

    Two industrial coal blends used in coke making were subjected to tests in order to assess the influence of waste sawdust (SC2 from chestnut and SP1 from pine) on the quality of the coke produced. The biomass was added in quantities of up to 5 wt.%. It was observed that biomass produced a substantial decrease in the plastic properties of the industrial coal blend, with reductions in Gieseler maximum fluidity of around 50% for 3 wt.% additions of the two different sawdusts. Carbonizations with ...

  2. Fundamentals of Delayed Coking Joint Industry Project

    Energy Technology Data Exchange (ETDEWEB)

    Volk Jr., Michael; Wisecarver, Keith D.; Sheppard, Charles M.

    2003-02-07

    The coking test facilities include three reactors (or cokers) and ten utilities. Experiments were conducted using the micro-coker, pilot-coker, and stirred-batch coker. Gas products were analyzed using an on-line gas chromatograph. Liquid properties were analyzed in-house using simulated distillation (HP 5880a), high temperature gas chromatography (6890a), detailed hydrocarbon analysis, and ASTM fractionation. Coke analyses as well as feedstock analyses and some additional liquid analyses (including elemental analyses) were done off-site.

  3. [Research on desulfurization using coke-oven wastewater with pulsed corona discharge].

    Science.gov (United States)

    Shao, Gui-wei; Li, Jin; Wang, Wan-lin; Li, Sheng-li

    2004-03-01

    A recent investigation into the application of pulsed corona discharge process, in which simultaneous SO2 removal from simulated flue gas and coke-oven wastewater degradation, was conducted at Wuhan Integrated Steel Plant. The outcome indicates that coke-oven wastewater had good desulfurization ability, and SO2 removal efficiency increased gradually as the simulated flue gas temperature increasing in the temperature range used during the experiment. When the flow of simulated flue gas was 428 m3/h, the temperature of simulated flue gas was 65 degrees C and coke-oven wastewater flow was 107 L/h, the desulfurization rate was 85%. Introducing pulsed corona discharge to the reactor enhanced the removal efficiencies of SO2, the desulfurization rate increased to 90% when high voltage was 52kV. When SO2 was removed from simulated flue gas by pulsed corona discharge, oil and phenols content in coke-oven wastewater decreased 39.26% and 68.75% respectively, and 99.98% content of cyanide was degraded, which is of important value in solving the inactivation problem of aerobic bacteria in biological treatment of coke-oven wastewater. PMID:15202239

  4. Coking wastewater increases micronucleus frequency in mouse in vivo via oxidative stress.

    Science.gov (United States)

    Zhu, Na; Li, Hongyan; Li, Guangke; Sang, Nan

    2013-10-01

    Coking wastewater has caused serious health risk in coal-producing areas of China, however its toxic effects have not been well understood. The genotoxicity induced by coking wastewater on mice in vivo and its possible oxidative mechanisms were investigated via observing the induction of micronuclei in polychromatic erythrocytes of mouse bone marrow, and subsequently determining the antioxidative enzyme activities (superoxide dismutase Cu, Zn-SOD, Se-dependent glutathione peroxidase, and catalase), thiobarbituric acid reactive substance contents and protein carbonyl levels in brains and livers of mice. Results showed that the tested coking wastewater caused a significant increase of micronucleus frequencies in a concentration-dependent manner. Also, the sample increased lipid peroxidation and protein oxidation levels, which was accompanied by changes in antioxidative status. Interestingly, pre-treatment with an antioxidant (vitamin C) led to a statistical reduction in the micronucleus frequency caused by coking wastewater. This implies that coking wastewater induces evident genetic damage in mammalian cells, and exposure to polluted areas might pose a potential genotoxic risk to human beings; in the process, oxidative stress played a crucial role. PMID:24494500

  5. A novel zeolite process for clean end use of hydrocarbon products

    Energy Technology Data Exchange (ETDEWEB)

    Keskinen, K.M. [Neste Oy, Porvoo (Finland). Technology Centre

    1996-12-31

    In recent years zeolites such as ZSM-5 have attracted considerable interest for the catalysis of a wide range of hydrocarbon transformations. A novel process developed by Neste converts light olefins to higher molecular weight hydrocarbon products. A wide range of high quality diesel, solvents and lube oils can be produced by the new NESKO process. Hydrotreated products have excellent properties; negligible sulphur or nitrogen compounds, very low aromatic content and pour point lower than -50 deg C. Proprietary technology is used in this olefin oligomerization process. (author) (7 refs.)

  6. Vadose Zone Clean Closure Report for the 300 Area Process Trenches

    International Nuclear Information System (INIS)

    This report documents the achievement of closure performance standards for the 300 Area Process Trenches (300 APT) located within the 300-FF-1 Operable Unit (OU). The report is intended to supplement the 300 Area Process Trenches Verification Package (BHI 1998C), which documents the achievement of the remedial action objectives specified in the 300-FF-1 Remedial Design Report/Remedial Action Work Plan (RDR/RAWP) (DOE-RL 1997). Upon acceptance of this document by the Washington State Department of Ecology, a 60-day period will begin to certify closure of the the process trenches

  7. Energy efficiency of alternative coke-free metallurgical technologies

    Energy Technology Data Exchange (ETDEWEB)

    V.G. Lisienko; A.V. Lapteva; A.E. Paren' kov [Ural State Technical University - Ural Polytechnic Institute, Yekaterinburg (Russian Federation)

    2009-02-15

    Energy analysis is undertaken for the blast-furnace process, for liquid-phase processes (Corex, Hismelt, Romelt), for solid-phase pellet reduction (Midrex, HYL III, LP-V in a shaft furnace), for steel production in systems consisting of a blast furnace and a converter, a Midrex unit and an arc furnace, or a Romelt unit and an arc furnace, and for scrap processing in an arc furnace or in an LP-V shaft furnace. Three blast-furnace processes with sinter and coke are adopted as the basis of comparison, as in: the standard blast-furnace process used in Russia; the improved blast-furnace process with coal-dust injection; and the production of vanadium hot metal from vanadium-bearing titanomagnetite ore (with a subsequent duplex process, ferrovanadium production, and its use in the arc furnace).

  8. Process and device for cleaning of water-containing machine oil from nuclear power plants

    International Nuclear Information System (INIS)

    The radioactive contaminants produced in water-containing machine oil in plants operated with nuclear power are removed from the contaminated machine oil by adsorption on water-adsorbing material. This document discusses this process. 3 figs., 1 tab

  9. NATO COMMITTEE ON THE CHALLENGES TO MODERN SOCIETY PILOT STUDY: CLEAN PRODUCTS AND PROCESSES

    Science.gov (United States)

    Promote cooperation for improving the common pollution landscape by stimulating cross-national dialogues and collaboration. Share knowledge on the methods, tools, and technologies for making cleaner products and processes possible.

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

    OpenAIRE

    Belošević Srđan V.; Tomanović Ivan D.; Crnomarković Nenad Đ.; Milićević Aleksandar R.; Tucaković Dragan R.

    2016-01-01

    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 c...

  11. The Value Proposition of 'Teck Coke Limited' Should Teck Enter the Coke Trade?

    OpenAIRE

    Colin Wilfred Petryk

    2011-01-01

    This paper will review the business case for Teck to enter the metallurgical cokemarket for the steel industry. The trend impacting investment is the growing demand forsteel. There are two coke battery technologies to choose from; environmental concernsmake the heat recovery oven the preferred technology. Four countries were considered inwhich to build the coke plant; Teck’s relationship with Chile and Chile’s desire forforeign investment makes it the best choice. Market size was estimated us...

  12. New systems for coke gas purification

    Energy Technology Data Exchange (ETDEWEB)

    Brodovich, A.I.; Zaichenko, V.M.; Melikentsova, V.I.; Shteinberg, E.A.

    1978-01-01

    Due to increased requirements for the purity of industrial emissions, recent years have seen further development of the new coke-oven gas purificaton methods which have been adopted by a number of plants. The improvement of these methods was caused by the necessity for solving problems of utilization or elimination of secondary production wastes.

  13. Automated combustion control of individual coke oven

    Energy Technology Data Exchange (ETDEWEB)

    Sumiso, Takashi; Watanabe, Yoshiaki; Yamate, Yoshitomo; Kawaguchi, Yasuhiro (Nippon Kokan Kabushiki Kaisha, Tokyo, Japan)

    1989-06-25

    NKK successfully developed an automated computerized combustion control system for coke oven for the first time in 1973. As the final stage of the development, an automated combustion control system for individual coke oven was completed and put to operation in July, 1988. The history of the development, method of combustion control and result of the operation are reported. In the earlier days, the automatic combustion control was made for a group of ovens, and 'combustion control of individual oven' was made by operators. Time series variation of flue temperatures of each oven is assumed to be the heat transfer from the combustion chamber to the carbonization chember which is treated as a function of assumed carbonization temperature, and expressed by a numerical model. The calculated target agreed well with the measured flue temperature. Temperature deviation for each flue is calculated every 2 hours, the degree of change is calculated, and the opening of the corresponding gas cock is automatically adjusted. The heat consumption showed a rapid decrease. The variation of coke strength decreased by 0.1 %, contributing very much for the reduction of coal cost for coke making. 7 figs., 1 tab.

  14. Simulation of transport phenomena in coke oven with staging combustion

    International Nuclear Information System (INIS)

    A three-dimensional transient mathematical model was developed for coupled coking chamber and staging combustion chamber in large-capacity coke ovens, to describe the flow–combustion–thermo behavior. The model was solved numerically using CFX CFD package and was validated by the central temperature evolution of coke bed. The fields of temperature, fluid flow and combustible gas concentration were analyzed, with special reference to the temperature difference of coke bed and NO concentration of exhaust. The results show that staging combustion plays an important role in improving temperature uniformity of the coke bed and reducing NO concentration of exhaust, especially for the large-capacity coke oven. It is beneficial for production optimization to decrease the gas mass flow rate at the bottom inlet while increase the rate at the upper inlet in the combustion chamber. In addition, it turns out that some measures such as coal preheating, adjustment of moisture content or/and coal densification may be used to improve the coke production efficiency. It is expected the developed model and relevant data in the present research will be beneficial to realize large-scale coke oven with a higher energy efficiency and lower emission. -- Highlights: • The application of staging combustion in coke ovens and its effects are analyzed. • A 3D model is proposed to describe flow–combustion–thermo behaviors in coke oven. • Optimizing operation parameters in full-scale coke oven are studied

  15. Coke Formation During Hydrocarbons Pyrolysis. Part Two: Methane Thermal Cracking Formation de coke pendant la pyrolyse des hydrocarbures. Deuxième partie : pyrolyse du méthane

    Directory of Open Access Journals (Sweden)

    Billaud F.

    2006-11-01

    Full Text Available Part one of this article dealt with coking in a steam cracking furnace. In this process, coke deposition is a very complex phenomenon due to the number of parameters involved. Nevertheless, for this process, coke deposition is a secondary reaction which does not affect steam cracking yields. It is completely different for methane thermal cracking. Coke is one of the main products of this reaction. Part two of this article deals with coke deposition on the walls of the reactors used for methane thermal cracking. After a brief description of the different set-ups used to study coke deposition, the main parameters involved are listed. The importance of temperature, conversion, type of diluent, and hydrocarbon partial pressure will be enhanced. To conclude, two approaches to the mechanism are proposed to explain coke formation during methane thermal cracking. La première partie de cet article faisait le point sur les réactions indésirables de cokage dans les réacteurs de vapocraquage : dans le cadre de ce procédé, la formation de coke est un phénomène complexe du fait du nombre important de paramètres mis en jeu. Toutefois, pour ce procédé, la réaction de formation du coke à la paroi des réacteurs est une réaction secondaire qui n'affecte pas les rendements de vapocraquage. Ceci est complètement différent dans le cas de la pyrolyse thermique du méthane, procédé pour lequel le coke est un produit principal et indésirable de la réaction. La seconde partie de cet article est consacrée plus particulièrement à la formation du coke, lors de la pyrolyse du méthane et présente les principaux résultats expérimentaux décrits dans la littérature. Parmi les différents montages expérimentaux utilisés pour mesurer le dépôt de coke, il est mentionné, à partir des travaux de la littérature, les 2 techniques suivantes : - la technique de la paroi chaude, - la technique du fil chaud. Pour la première technique, les montages exp

  16. Prediction of the quality of coke obtained from vacuum residues by using spectroscopy infrared FTIR-ART

    Science.gov (United States)

    León, A. Y.; Rodríguez, N. A.; Mejía, E.; Cabanzo, R.

    2016-02-01

    According to the trend of the heavy crudes and high demand of fuels, it is projected a considerable increase in the production of vacuum residues. With the purpose of taking advantage of these loads, the refineries have been improving conversion processes for the production of better quality distillates. However, as increasing the severity conditions and the species content of resins and asphaltenes high concentrations of coke are obtained. To provide an insight into the quality and cokes properties, in this study fifty (50) coke samples obtained from vacuum residues processed under conditions of thermal cracking and hydroconversion were selected. Each coke was analysed in detail with properties such as fixed carbon, volatile material, ash, and calorific value. Subsequently, a characterization methodology was developed to predict the properties of cokes, by using partial least squares regression, and infrared spectroscopy (FTIR-ATR) in the spectral range from 4000 to 500cm-1. The models obtained by chemometrics allowed to predict the quality of the coke produced from vacuum residues with reliable responses in short periods of time.

  17. [Preliminary investigation on emission of PCDD/Fs and DL-PCBs through flue gas from coke plants in China].

    Science.gov (United States)

    Sun, Peng-Cheng; Li, Xiao-Lu; Cheng, Gang; Lu, Yong; Wu, Chang-Min; Wu, Chang-Min; Luo, Jin-Hong

    2014-07-01

    According to the Stockholm Convention, polychlorinated dibenzo-p-dioxins/dibenzofurans (PCDD/Fs) and dioxin-like polychlorinated biphenyls (DL-PCBs) are classified into unintentionally produced persistent organic pollutants (UP-POPs), and named dioxins. Coke production as a thermal process contains organic matters, metal and chlorine, is considered to be a potential source of dioxins. Intensive studies on the emission of dioxins from coking industry are still very scarce. In order to estimate the emission properties of dioxins through coke production, isotope dilution HRGC/HRMS technique was used to determine the concentration of dioxins through flue gas during heating of coal. Three results were obtained. First, total toxic equivalents at each stationary emission source were in the range of 3.9-30.0 pg x m(-3) (at WHO-TEQ) for dioxins which was lower than other thermal processes such as municipal solid waste incineration. Second, higher chlorinated PCDD/Fs were the dominant congeners. Third, emissions of dioxins were dependent on coking pattern. Stamping coking and higher coking chamber may lead to lower emission. PMID:25244832

  18. Coking coals of Mongolia: Distribution and resources

    Science.gov (United States)

    Erdenetsogt, Bat-Orshikh; Jargal, Luvsanchultem

    2016-04-01

    The coal deposits of Mongolia tend to become younger from west to east and can be subdivided into two provinces, twelve basins, and three areas. Main controlling factor of coal rank is the age of coal bearing sequences. Western Mongolian coal-bearing province contains mostly high rank bituminous coal in strata from Late Carboniferous. The basins in southern Mongolia and the western part of central Mongolia have low rank bituminous coal in strata from the Permian. The northern and central Mongolian basins contain mainly Jurassic subbituminous coal, whereas the Eastern Mongolian province has Lower Cretaceous lignite. Mongolian known coking coal reserves are located in western, southern and northern Mongolia and related to Carboniferous, Permian and Jurassic sequences, respectively. Pennsylvanian Nuurstkhotgor coal deposit is located in northwestern Mongolia (in Western Mongolian coal-bearing province). The coals have 1-7.5 crucible swelling number (CSN) and 0-86 G-index. Vitrinite reflectance value (Rmax in oil) varies from 0.7% to 1.2% and sulfur content is low, ranging from 0.3% to 0.6% with an average of 0.4%. Coal reserve is estimated to be 1.0 billion ton, of which half is coking coal. Upper Permian Khurengol deposit is situated in western Mongolia (in Western Mongolian coal-bearing province). CSN and G-index of coal are 8-9 and 54-99, respectively. The coals have Rmax of 1.1 to 1.7% (average 1.4%) and sulfur content of 0.2 to 0.6% (average 0.4%). Coking coal reserve of the deposit is estimated to be 340 million ton. Upper Permian Tavantolgoi, the largest coking coal deposit, lies in southern Mongolia (in South Gobi coal-bearing basin). The coals have CSN of 1 to 7.5 and Rmax of 0.7% to 1.2%. Sulfur content is low, ranging from 0.5% to 0.9%. Coal reserve is estimated to be 6.0 billion ton, of which 2.0 billion ton is accounted as coking coal. Lower-Middle Jurassic Ovoot coal is located in northern Mongolia (in Orkhon-Selenge coal-bearing area). This is one of

  19. Thermal coupling between crude distillation and delayed coking units

    Energy Technology Data Exchange (ETDEWEB)

    Plesu, V.; Bumbac, G.; Iancu, P. [University Politechnica of Bucharest (Romania). Centre for Technology Transfer in the Process Industries; Ivanescu, I. [SNP PETROM, Bucharest (Romania); Popescu, D.C. [SNP PETROM, INCERP Ploiesti Subsidiary, Ploiesti (Romania)

    2003-10-01

    The paper presents an industrial case study. Crude distillation unit (CDU) and delayed coking unit (DCU) are important plants in oil refineries, presenting huge energy consumption, especially due to high flowrates of process material streams. Any acceptable solution for energy saving is important in this context. The idea of thermal coupling between these two plants is good as they have potential to exchange energy, but the problem is to choose the most appropriate way to do it. The objective of this work is to present the possibility to exchange energy between the two plants, continuing a previous work [Energy saving by integration of CDU-delayed coke plants, third Conference, Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction - PRES 2000, P7.72], where a part of the solution was already presented. The difficulty to find a solution arisen from the fact that DCU is working semi-continuous. More insights in the process allowed finding new possibilities, more attractive for rational use of energy, with better applicability. A feasibility study will be performed to give also economic sound of all the implications for the modifications proposed. (author)

  20. Development of coke oven combustion control technology (III). Development of a control system for coke oven combustion

    Energy Technology Data Exchange (ETDEWEB)

    Ono, M.; Yamamura, H.; Yamamoto, T.; Miyake, M.; Itoh, Y.; Yamashita, H.

    1983-01-01

    A 41 gate combustion control system has been developed at Sumitomo Chemicals' Kashima II - D coke oven battery as a means of stabilizing coke quality and reducing the amount of heat required for coking. The system has been operating smoothly since January 1983. Low level stability of oven temperature has been obtained and the variation in coking times among the ovens has been reduced. The coking heat requirement has been decreased by approximately 20 kcal/kg-coal. The control functions of the system and the control model upon which it is based are indicated, and control results are given.

  1. The effect of high and low dissolved oxygen on the toxicity of oil sands coke and its leachate to Chironomus tentans

    International Nuclear Information System (INIS)

    A study was conducted to assess the effect of low dissolved oxygen on the long-term leaching potential of the toxic constituents found in coke. Coke is one of the waste products produced during the oil sand upgrading process used at Syncrude Canada Ltd. and Suncor Energy Inc. Coke is contaminated by metals and organic compounds which can leach into the environment. In this study, coke from both companies was exposed to reconstituted water and high dissolved oxygen for a period of 30 days, during which time the overlying water containing the leachate and the coke pore-water was chemically analyzed. The benthic macroinvertebrate, Chironomus tentans, was exposed to the aged coke and the overlying leachate after the 30 day period. The study did not reveal any major difference in the survival or growth between the dissolved oxygen treatments or any of the leachate treatments. The macroinvertebrate in the aged Syncrude grew significantly while the Suncor coke strongly inhibited both survival and growth of the macroinvertebrate. The study demonstrates that coke has the potential to negatively affect benthic organisms if it is used uncovered in an aquatic reclamation effort

  2. 配型煤炼焦技术的研究与实践%Research and Practice of Coal Blending Coking Technology

    Institute of Scientific and Technical Information of China (English)

    高丽

    2013-01-01

    Coal blending coking technology could improve the adhesion of coal, enhanced coke strength, high quality coal resource saving. Paper analyzed properties of coking coal blending for coking coal mechanism, introduced Nippon Steel iftted with Sumitomo Metal and coal briquette coke making process, as well as various coking plants matched the result through the coke oven experiment and the production practice which the coal coking obtained.%配型煤炼焦技术可以改善煤料的粘结性,增强焦炭强度,节约优质煤资源。文章分析了配型煤炼焦对炼焦煤料性能的影响机理,介绍了新日铁配型煤和住友金属配型煤炼焦工艺,以及各焦化厂通过焦炉实验和生产实践总结的配型煤炼焦的结果。

  3. Effect of pre-oxidization on the cyclic coking and carburizing resistance of HP40 alloy: With and without yttrium modification

    International Nuclear Information System (INIS)

    Highlights: •The integrity oxide layer retards the coking and carburizing process. •The oxide scale changed the carbon deposited mechanism. •Lower coking speed induces lower thermal stress during cyclic carburizing. •Higher pre-oxidation temperature deteriorates the carburizing resistance. •Yttrium addition can sustain the oxide scale integrity during the carburizing. -- Abstract: The pre-oxidation results demonstrate that rare earth elements play an important role on the scale adherence of alloy after the oxidation at elevated temperature. The better scale adherence of the yttrium modified alloy permits a superior cyclic coking and carburizing resistance. This is because the integrity chromia layer, which prevents fast ion diffusion, can retard the outer catalytic coking and the inner carburizing of pre-oxidized alloy. As for the alloy under the cast condition, severe coking and carburization has been detected, which was also observed on the pre-oxidized samples where the scale suffered from severe spalling

  4. Characterized and cleaning process of montmorillonite clay from Parelhas, Rio Grande do Norte state, Brazil

    International Nuclear Information System (INIS)

    The application of montmorillonite nano composites has been improved in order to obtain dispersed phase with particles of nano metric dimensions. To obtain these nanoparticles, the clays must pass an effective purification process for removing unwanted materials, which would undermine the processes of intercalation and exfoliation of montmorillonite in a polymer matrix. This study intention to characterize and purify a montmorillonite clay from deposit recently discovered in the city of Parelhas in Rio Grande do Norte, through the separation of coarser materials by decantation followed by a chemical attack that promoted oxidation in samples where it was realized reduction of impurities such as organic matter and other substances that would hinder the achievement of nanoparticles. Under these conditions, the clay is suitable for the work as dispersed phase in a polymer matrix nano composite. The results were demonstrated by analysis of scanning electron microscopy (SEM), chemical analysis, BET and X-ray diffraction (XRD). (author)

  5. Biomass Gasification - Process analysis and dimensioning aspects for downdraft units and gas cleaning lines

    OpenAIRE

    Stoppiello, Giovanni

    2010-01-01

    In such territories where food production is mostly scattered in several small / medium size or even domestic farms, a lot of heterogeneous residues are produced yearly, since farmers usually carry out different activities in their properties. The amount and composition of farm residues, therefore, widely change during year, according to the single production process periodically achieved. Coupling high efficiency micro-cogeneration energy units with easy handling biomass conversion equipm...

  6. 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

  7. Charge generation associated with liquid spraying in tank cleaning and comparable processes - preliminary experiments

    Science.gov (United States)

    Blum, Carsten; Losert, Oswald F. J.

    2015-10-01

    The BG RCI has initiated investigations in order to improve the data basis for assessing the ignition hazard by electrostatic charging processes associated with the spraying of liquids. On the base of preliminary experiments, we established procedures for measurements of electric field strength and charging current in the presence of aerosol particles. Results obtained with three different nozzle types, variation of pressure and with built-in deflecting plate are presented.

  8. New characterisation tests of the coke behaviour at high temperature

    Energy Technology Data Exchange (ETDEWEB)

    Danloy, G.; Pesneux, P.; Fischbach, J.P. (and others) [CRM, Liege (Belgium)

    2009-07-01

    New laboratory tests have been developed to characterise the coke behaviour at high temperature under conditions similar to those encountered in the blast furnace, especially in terms of gasification degree. The CRM Cokarac test characterises the evolution of coke size distribution under mechanical, chemical and thermal stresses during increasing residence time under gasification conditions prevailing in the blast furnace. Two Corus tests characterise the resistance of coke submitted to the actions of liquid iron and slag. A CPM test characterises the strength of coke after a constant weight loss. The validity of these new tests has been demonstrated by comparing the modifications of the coke grain size and microscopic texture resulting from the tests with those undergone by coke in the blast furnace. The latter have been measured by comparing cokes sampled by a tuyere probe with cokes sampled before charging into the blast furnace. Industrial cokes from a wide variety of sources have been tested. Moreover, to highlight the sensitivity of the new tests and their innovative content, cokes differing greatly by their CRI and CSR indices have been produced in the pilot coke oven plant of CPM. The results of the new tests showed only little correlation with the classical coke characterisation indices (I10, I40) and with the standard CRI-CSR indices, which indicates that they really bring new information on coke properties. The applicability of these new tests on a routine basis has been evaluated in order to allow the ironmaking industry to better characterise coke quality. 15 refs., 90 figs., 23 tabs., 13 apps.

  9. Problem Analysis and Improvement in Stamping Coke Production by Transformed Top Charging Coke Oven%顶装焦炉改为捣固焦生产后的问题及改进

    Institute of Scientific and Technical Information of China (English)

    王即胜; 刘成雷; 常宇

    2014-01-01

    In order to reduce production cost, Jinan Steel transformed three 4.3 m top charging coke ovens for stamping coke production. Because of relatively small shrinkage of the coal in coking process, imperfect transformation facilities, unreasonable operation and other reasons, some problems appeared in the production, for example, large coke pushing current, serious leaking of oven body and poor dedusting effect. By controlling the G value of mixed coal below 72, reducing the density of briquette heap, narrowing the width of briquettes and other measures, the existent problems were avoided or relieved. In view of different structure and production characteristics between top charging coke oven and tamping coke oven, caution should be taken in the top charging coke oven transformed to tamping coke production.%为降低生产成本,济钢将3座4.3 m顶装焦炉改为捣固焦生产。由于入炉煤在结焦过程中收缩量相对变小,配套设施改造不完善,操作不合理等原因,导致生产中出现推焦电流过大、炉体窜漏严重、除尘效果差等问题。通过控制配合煤G值在72以下,降低煤饼堆比重,缩小煤饼宽度等措施,存在的问题得到了避免或缓解。鉴于顶装焦炉和捣固焦炉不同的结构及生产特点,应谨慎考虑顶装焦炉改捣固焦生产。

  10. Biofilms of Enterococcus faecalis and Enterococcus faecium isolated from the processing of ricotta and the control of these pathogens through cleaning and sanitization procedures.

    Science.gov (United States)

    da Silva Fernandes, Meg; Kabuki, Dirce Yorika; Kuaye, Arnaldo Yoshiteru

    2015-05-01

    The biofilm formation of Enterococcus faecalis and Enterococcus faecium isolated from the processing of ricotta on stainless steel coupons was evaluated, and the effect of cleaning and sanitization procedures in the control of these biofilms was determined. The formation of biofilms was observed while varying the incubation temperature (7, 25 and 39°C) and time (0, 1, 2, 4, 6 and 8 days). At 7°C, the counts of E. faecalis and E. faecium were below 2 log10 CFU/cm(2). For the temperatures of 25 and 39°C, after 1 day, the counts of E. faecalis and E. faecium were 5.75 and 6.07 log10 CFU/cm(2), respectively, which is characteristic of biofilm formation. The tested sanitation procedures a) acid-anionic tensioactive cleaning, b) anionic tensioactive cleaning+sanitizer and c) acid-anionic tensioactive cleaning+sanitizer were effective in removing the biofilms, reducing the counts to levels below 0.4 log10 CFU/cm(2). The sanitizer biguanide was the least effective, and peracetic acid was the most effective. These studies revealed the ability of enterococci to form biofilms and the importance of the cleaning step and the type of sanitizer used in sanitation processes for the effective removal of biofilms. PMID:25702883

  11. Clean-up and processing of coal-derived gas for hydrogen applications

    Science.gov (United States)

    Kasper, S.

    It appears that only a few large-scale industrial applications need to be examined for utilization of coal-derived hydrogen. Applications selected as representative for considerations of purification are related to ammonia, methanol, iron ore reduction, fuel cells, and pipeline gas. Purity requirements and raw gas composition are discussed, and a description of purification processes is provided. Attention is given to particulates, tar, ammonia and water, light oils, bulk acid gas removal, trace sulfur removal, carbon monoxide, hydrogen cyanide, cryogenic purification, and molecular sieves. In view of the very high purity requirements for many hydrogen applications, and the variety of undesirable components in the raw coal gas, the purification task may seem to be too formidable. However, the utilization of hydrogen gas for the production of methanol and ammonia in many countries proves that such a purification is economically feasible.

  12. Process development studies on recovery of clean coal from ultra fine hardcoal tailings using enhanced gravity separator

    Energy Technology Data Exchange (ETDEWEB)

    Ozgen, S.; Turksoy, V.O.; Sabah, E.; Oruc, F. [Afyon Kocatepe Univ., Afyonkarahisar (Turkey). Dept. of Mining Engineering

    2009-10-15

    Gravity-based processing methods were used to process and recover clean coal from ultra-fine hardcoal tailings at a site in Turkey. The coal samples were analyzed using X-ray diffraction and X-ray fluorescence. A hydrocyclone was used to conduct classification tests and to separate the clay minerals from the coal. The effects of various operating parameters were also investigated. Regression analysis was used to characterize the relationship between the ash content and coal recovery rate and the feed solid, inlet pressure, diameter of vortex, and diameter of apex variables of the hydrocyclone. The effects of feed pressure were also investigated. The study showed that coal can be economically recovered from hardcoal tailings containing clay minerals. It was concluded that a coal sample with 6.98 per cent ash content and a net calorific value of 28,778 kJ was obtained with a weight recovery of 61.73 per cent. 25 refs., 8 tabs., 18 figs.

  13. Reaction Mechanism for the Formation of Nitrogen Oxides (NO x ) During Coke Oxidation in Fluidized Catalytic Cracking Units

    KAUST Repository

    Chaparala, Sree Vidya

    2015-06-11

    Fluidized catalytic cracking (FCC) units in refineries process heavy feedstock obtained from crude oil distillation. While cracking feed, catalysts get deactivated due to coke deposition. During catalyst regeneration by burning coke in air, nitrogen oxides (NOx) are formed. The increase in nitrogen content in feed over time has resulted in increased NOx emissions. To predict NOx concentration in flue gas, a reliable model for FCC regenerators is needed that requires comprehensive understanding and accurate kinetics for NOx formation. Based on the nitrogen-containing functional groups on coke, model molecules are selected to study reactions between coke-bound nitrogen and O2 to form NO and NO2 using density functional theory. The reaction kinetics for the proposed pathways are evaluated using transition state theory. It is observed that the addition of O2 on coke is favored only when the free radical is present on the carbon atom instead of nitrogen atom. Thus, NOx formation during coke oxidation does not result from the direct attack by O2 on N atoms of coke, but from the transfer of an O atom to N from a neighboring site. The low activation energies required for NO formation indicate that it is more likely to form than NO2 during coke oxidation. The favorable pathways for NOx formation that can be used in FCC models are identified. Copyright © 2015 Taylor & Francis Group, LLC.

  14. Clean coal initiatives in Indiana

    Science.gov (United States)

    Bowen, B.H.; Irwin, M.W.; Sparrow, F.T.; Mastalerz, Maria; Yu, Z.; Kramer, R.A.

    2007-01-01

    Purpose - Indiana is listed among the top ten coal states in the USA and annually mines about 35 million short tons (million tons) of coal from the vast reserves of the US Midwest Illinois Coal Basin. The implementation and commercialization of clean coal technologies is important to the economy of the state and has a significant role in the state's energy plan for increasing the use of the state's natural resources. Coal is a substantial Indiana energy resource and also has stable and relatively low costs, compared with the increasing costs of other major fuels. This indigenous energy source enables the promotion of energy independence. The purpose of this paper is to outline the significance of clean coal projects for achieving this objective. Design/methodology/approach - The paper outlines the clean coal initiatives being taken in Indiana and the research carried out at the Indiana Center for Coal Technology Research. Findings - Clean coal power generation and coal for transportation fuels (coal-to-liquids - CTL) are two major topics being investigated in Indiana. Coking coal, data compilation of the bituminous coal qualities within the Indiana coal beds, reducing dependence on coal imports, and provision of an emissions free environment are important topics to state legislators. Originality/value - Lessons learnt from these projects will be of value to other states and countries.

  15. Recleaning of HEPA filters by reverse flow - evaluation of the underlying processes and the cleaning technique

    International Nuclear Information System (INIS)

    HEPA filter operation at high concentrations of fine dusts requires the periodic recleaning of the filter units in their service locations. Due to the low mechanical stress induced during the recleaning process the regenration via low pressure reverse flow is a very suitable technique. Recleanability of HEPA filter had been attained for particle diameter >0,4 μm at air velocities up to 1 m/s, but filter clogging occurred in case of smaller particles. The recleaning forces are too weak for particles <0,4 μm. With respect to the low tensile strength of HEPA filter media higher flow velocities are excluded. The analysis of reverse flow recleaning in a single pleat device showed extremly non uniform flow pattern in conventional deep-pleat pack geometries. More uniform flow conditions are attained by changing the pleat geometry. The realisation of high flow velocities at the glas fiber medium inside the filter pack requires shortening of the pleates to some 150 mm and the adaptation of the distance between filter pack and the recleaning device with respect to the nozzle diameter and the width of the filter pleats. (orig.). 44 figs., 36 refs

  16. Automatic operation systems for the coke oven top; Cokes ro rojo sagyo no jidoka tachiage jokyo

    Energy Technology Data Exchange (ETDEWEB)

    Saji, T.; Kitayama, Y. [Sumitomo Metal Industries, Ltd., Osaka (Japan)

    1994-10-13

    This paper describes an outline of automatic operation on the coke oven top, which has been conducted at the Kashima Steel Works, Sumitomo Metal Industries, Ltd. For the automatic operation on the oven top, unmanned operation of the charging car, mechanization of works on the oven top, centralized control, and simplification of the system were introduced. This automatic system consists of the charging car, central station, charging car station, and quenching car automation system. For the automatic travel motion control, braking by the electric regenerative brake and disk brake was adopted. The oven center standing control is carried out by using the position and distance information of interlock cable and the oven center sensor. Standing accuracy of the oven center of charging car was designed to be up to {plus_minus}10 mm. High detection accuracy can be obtained through the optical cutting image processing. The carbon removing apparatus for inlet port, oven top cleaner dust treatment apparatus, and charging level measurement apparatus were added to the charging car, which were required for the automatic operation on the oven top. As a result, the automatic ratio more than 99% could be achieved. 6 figs., 4 tabs.

  17. The Effect of Process Condition and SiO2 as Catalyst for the Density and the Resistivity of the Calcine Coke and Tar Pitch Mixed Pellet as 900 oC Baking Product

    International Nuclear Information System (INIS)

    The experiment of the baking condition effect and SiO2 as catalyst have been done. Graphite turbo static be produced by baking of the mixed pellet ( Calcine Coke, Tar Pitch (32%) and SiO2 as catalyst). The baking have been done on the inert atmospherics (argon : 2 l/hour) and the heating rate 10 oC/minute. The baking condition and catalyst was affected for density and resistivity. There was little bit density change with densification phenomena. The graphite resistivity was more decrease with the increasing of heating and the longer baking time. The baking condition for produce turbo static graphite with resistivity 2100 Ωμm and density 1.4 gram/cm3 was 900 oC, 3 hours for baking time and optimal adding catalyst SiO2 0.5 %. (author)

  18. Clean Coal Technology Demonstration Program. Program update 1994

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1995-04-01

    The Clean Coal Technology Demonstration Program (CCT Program) is a $7.14 billion cost-shared industry/government technology development effort. The program is to demonstrate a new generation of advanced coal-based technologies, with the most promising technologies being moved into the domestic and international marketplace. Clean coal technologies being demonstrated under the CCT program are creating the technology base that allows the nation to meet its energy and environmental goals efficiently and reliably. The fact that most of the demonstrations are being conducted at commercial scale, in actual user environments, and under conditions typical of commercial operations allows the potential of the technologies to be evaluated in their intended commercial applications. The technologies are categorized into four market sectors: advanced electric power generation systems; environmental control devices; coal processing equipment for clean fuels; and industrial technologies. Sections of this report describe the following: Role of the Program; Program implementation; Funding and costs; The road to commercial realization; Results from completed projects; Results and accomplishments from ongoing projects; and Project fact sheets. Projects include fluidized-bed combustion, integrated gasification combined-cycle power plants, advanced combustion and heat engines, nitrogen oxide control technologies, sulfur dioxide control technologies, combined SO{sub 2} and NO{sub x} technologies, coal preparation techniques, mild gasification, and indirect liquefaction. Industrial applications include injection systems for blast furnaces, coke oven gas cleaning systems, power generation from coal/ore reduction, a cyclone combustor with S, N, and ash control, cement kiln flue gas scrubber, and pulse combustion for steam coal gasification.

  19. The shell coal gasification process

    Energy Technology Data Exchange (ETDEWEB)

    Koenders, L.O.M.; Zuideveld, P.O. [Shell Internationale Petroleum Maatschappij B.V., The Hague (Netherlands)

    1995-12-01

    Future Integrated Coal Gasification Combined Cycle (ICGCC) power plants will have superior environmental performance and efficiency. The Shell Coal Gasification Process (SCGP) is a clean coal technology, which can convert a wide range of coals into clean syngas for high efficiency electricity generation in an ICGCC plant. SCGP flexibility has been demonstrated for high-rank bituminous coals to low rank lignites and petroleum coke, and the process is well suited for combined cycle power generation, resulting in efficiencies of 42 to 46% (LHV), depending on choice of coal and gas turbine efficiency. In the Netherlands, a 250 MWe coal gasification combined cycle plant based on Shell technology has been built by Demkolec, a development partnership of the Dutch Electricity Generating Board (N.V. Sep). The construction of the unit was completed end 1993 and is now followed by start-up and a 3 year demonstration period, after that the plant will be part of the Dutch electricity generating system.

  20. Laser surface cleaning

    International Nuclear Information System (INIS)

    The objective of this work is a laboratory demonstration that red-lead primer and two-part epoxy paints can be stripped from concrete and metal surfaces using surface cleaning systems based on pulsed-repetition CO2 lasers. The three goals are to: (1) demonstrate coatings removal, including surface pore cleaning; (2) demonstrate that there is negligible release of ablated contaminants to the environment; and (3) demonstrate that the process will generate negligible amounts of additional waste compared to competing technologies. Phase 1 involved site visits to RMI and Fernald to assess the cleaning issues for buildings and parts. In addition, Phase 1 included detailed designs of a more powerful system for industrial cleaning rates, including laser, articulating optics, ablated-material capture suction nozzle attached to a horizontal raster scanner for floor cleaning, and filtration system. Some concept development is also being done for using robots, and for parts cleaning. In Phase 2 a transportable 6 kW system will be built and tested, with a horizontal surface scanner for cleaning paint from floors. The laboratory tests will again be instrumented. Some concept development will continue for using robots, and for parts cleaning. This report describes Phase 1 results

  1. Thermalhydraulic assessment of the Pickering NGS 'B' feed and bleed system for the hot boiler chemical clean (Siemens Process)

    International Nuclear Information System (INIS)

    The Hot Boiler Chemical Clean (HBCC) process from Siemens, to be used in PNGS, requires that the Heat Transport System (HTS) temperature be maintained in the range 160 to 170 oC for several days. To achieve these thermalhydraulic condition, the core decay power and the pump power of the main circulating pumps in a 3-3 configuration are employed to warm up the HTS from approximately 38 oC to 170 oC. At this point, high Bleed bias is applied to the signal of the HTS pressure controller to provide high Feed and Bleed flows, which are used to control the HTS temperature by means of the Bleed Cooler. To address any concern posed by these infrequently used HTS thermalhydraulic conditions, a detailed thermalhydraulic model of the Feed and Bleed System, that also includes the Gland Supply, Gland Return and Purification systems, was developed for the TUF code to determine the suitability of the Feed and Bleed System to conduct the HBCC. The model was then used to estimate the parameters such as Feed and Bleed flows, valve openings, pressure and temperature distributions throughout the Feed and Bleed System required for the application of HBCC. (author)

  2. Polyaniline-Coated Carbon Nanotube Ultrafiltration Membranes: Enhanced Anodic Stability for In Situ Cleaning and Electro-Oxidation Processes.

    Science.gov (United States)

    Duan, Wenyan; Ronen, Avner; Walker, Sharon; Jassby, David

    2016-08-31

    Electrically conducting membranes (ECMs) have been reported to be efficient in fouling prevention and destruction of aqueous chemical compounds. In the current study, highly conductive and anodically stable composite polyaniline-carbon nanotube (PANI-CNT) ultrafiltration (UF) ECMs were fabricated through a process of electropolymerization of aniline on a CNT substrate under acidic conditions. The resulting PANI-CNT UF ECMs were characterized by scanning electron microscopy, atomic force microscopy, a four-point conductivity probe, cyclic voltammetry, and contact angle goniometry. The utilization of the PANI-CNT material led to significant advantages, including: (1) increased electrical conductivity by nearly an order of magnitude; (2) increased surface hydrophilicity while not impacting membrane selectivity or permeability; and (3) greatly improved stability under anodic conditions. The membrane's anodic stability was evaluated in a pH-controlled aqueous environment under a wide range of anodic potentials using a three-electrode cell. Results indicate a significantly reduced degradation rate in comparison to a CNT-poly(vinyl alcohol) ECM under high anodic potentials. Fouling experiments conducted with bovine serum albumin demonstrated the capacity of the PANI-CNT ECMs for in situ oxidative cleaning, with membrane flux restored to its initial value under an applied potential of 3 V. Additionally, a model organic compound (methylene blue) was electrochemically transformed at high efficiency (90%) in a single pass through the anodically charged ECM. PMID:27525344

  3. Electron-beam-induced deposition and post-treatment processes to locally generate clean titanium oxide nanostructures on Si(100)

    Science.gov (United States)

    Schirmer, M.; Walz, M.-M.; Vollnhals, F.; Lukasczyk, T.; Sandmann, A.; Chen, C.; Steinrück, H.-P.; Marbach, H.

    2011-02-01

    We have investigated the lithographic generation of TiOx nanostructures on Si(100) via electron-beam-induced deposition (EBID) of titanium tetraisopropoxide (TTIP) in ultra-high vacuum (UHV) by scanning electron microscopy (SEM) and local Auger electron spectroscopy (AES). In addition, the fabricated nanostructures were also characterized ex situ via atomic force microscopy (AFM) under ambient conditions. In EBID, a highly focused electron beam is used to locally decompose precursor molecules and thereby to generate a deposit. A drawback of this nanofabrication technique is the unintended deposition of material in the vicinity of the impact position of the primary electron beam due to so-called proximity effects. Herein, we present a post-treatment procedure to deplete the unintended deposits by moderate sputtering after the deposition process. Moreover, we were able to observe the formation of pure titanium oxide nanocrystals (<100 nm) in situ upon heating the sample in a well-defined oxygen atmosphere. While the nanocrystal growth for the as-deposited structures also occurs in the surroundings of the irradiated area due to proximity effects, it is limited to the pre-defined regions, if the sample was sputtered before heating the sample under oxygen atmosphere. The described two-step post-treatment procedure after EBID presents a new pathway for the fabrication of clean localized nanostructures.

  4. Electron-beam-induced deposition and post-treatment processes to locally generate clean titanium oxide nanostructures on Si(100)

    Energy Technology Data Exchange (ETDEWEB)

    Schirmer, M; Walz, M-M; Vollnhals, F; Lukasczyk, T; Sandmann, A; Steinrueck, H-P; Marbach, H [Lehrstuhl fuer Physikalische Chemie II and Interdisciplinary Center for Molecular Materials (ICMM), Universitaet Erlangen-Nuernberg, Egerlandstrasse 3, D-91058 Erlangen (Germany); Chen, C, E-mail: marbach@chemie.uni-erlangen.de [Department of Chemistry, Stanford University, Stanford, CA 94305 (United States)

    2011-02-25

    We have investigated the lithographic generation of TiO{sub x} nanostructures on Si(100) via electron-beam-induced deposition (EBID) of titanium tetraisopropoxide (TTIP) in ultra-high vacuum (UHV) by scanning electron microscopy (SEM) and local Auger electron spectroscopy (AES). In addition, the fabricated nanostructures were also characterized ex situ via atomic force microscopy (AFM) under ambient conditions. In EBID, a highly focused electron beam is used to locally decompose precursor molecules and thereby to generate a deposit. A drawback of this nanofabrication technique is the unintended deposition of material in the vicinity of the impact position of the primary electron beam due to so-called proximity effects. Herein, we present a post-treatment procedure to deplete the unintended deposits by moderate sputtering after the deposition process. Moreover, we were able to observe the formation of pure titanium oxide nanocrystals (<100 nm) in situ upon heating the sample in a well-defined oxygen atmosphere. While the nanocrystal growth for the as-deposited structures also occurs in the surroundings of the irradiated area due to proximity effects, it is limited to the pre-defined regions, if the sample was sputtered before heating the sample under oxygen atmosphere. The described two-step post-treatment procedure after EBID presents a new pathway for the fabrication of clean localized nanostructures.

  5. Patterning of gold nano-octahedra using electron irradiation combined with thermal treatment and post-cleaning process

    International Nuclear Information System (INIS)

    A novel approach to pattern nanocrystalline gold (Au) octahedra is presented based on electron irradiation combined with thermal treatment and post-cleaning process using HAuCl4-loaded poly(styrene-b-2-vinyl pyridine) (PS-b-P2VP) block copolymer (BCP) as a precursor material. The BCP tends to cross-link under electron irradiation, and thus a patterned film can be prepared by selectively irradiating an electron beam onto a precursor film using a shadow mask. A post-thermal treatment leads to the formation of crystalline Au nano-octahedra inside the patterned film with a help of the BCP acting as a capping agent. Subsequently, the BCP can be removed by O2 plasma etching combined with oxidative degradation, with the Au nanoparticles remaining. As a result, a patterned film consisting of high-purity nanocrystalline Au octahedra is fabricated. The sizes of the Au octahedral nanoparticles can be readily controlled from 49 to 101 nm by changing the thickness of the precursor film. The patterned Au nano-octahedra films exhibit excellent surface-enhanced Raman scattering behavior with the maximum enhancement factor of ∼106.

  6. The Transient Modal Dynamic Analysis of a Coke Tower

    Institute of Scientific and Technical Information of China (English)

    XIE Teng-teng; SUN Tie; XING Ling; ZHANG Su-xiang

    2012-01-01

    Dynamic analysis must be performed when the duration of the applied load is short or if the load is dynamic in nature. Wind load, as a random load, can lead to the vibration of the coke tower. In order to study the influence to the strength of the coke tower by wind, ABAQUS was used to conduct the transient modal dynamic analysis of the wind load. The response of the structure during loading and unloading was mainly observed. The results indicate that, with the effect of wind, the maximal nodal displacement appears at the top of the tower, which is 0.79 mm; while the maximal stress locates at the node around the skirt, the maximum is 3.26 MPa. Both of the displacement and stress cannot cause the failure of the structure. After loading and unloading, the structure engenders vibration along the loading direction. The frequency is 10 Hz, under the effect of external loads, it may easily cause the resonance of the structure, which can cause damage to the structure. So it must be taken into consideration during the process of design and operation.

  7. Treatment of coking wastewater by using manganese and magnesium ores

    Energy Technology Data Exchange (ETDEWEB)

    Chen Tianhu; Huang Xiaoming; Pan Min [School of Resources and Environmental Engineering, Hefei University of Technology, Hefei City 230009 (China); Jin Song, E-mail: sjin@uwyo.edu [MWH Americas, 3665 JFK Parkway, Suite 206, Fort Collins, CO 80525 (United States); Department Civil and Architectural Engineering, University of Wyoming, Laramie, WY 82071 (United States); Peng Suchuan [School of Resources and Environmental Engineering, Hefei University of Technology, Hefei City 230009 (China); Fallgren, Paul H. [Western Research Institute, 365 North 9th Street, Laramie, WY 82072 (United States)

    2009-09-15

    This study investigated a wastewater treatment technique based on natural minerals. A two-step process using manganese (Mn) and magnesium (Mg) containing ores were tested to remove typical contaminants from coking wastewater. Under acidic conditions, a reactor packed with Mn ore demonstrated strong oxidizing capability and destroyed volatile phenols, chemical oxygen demand (COD){sub ,} and sulfide from the coking wastewater. The effluent was further treated by using Mg ore to remove ammonium-nitrogen and phosphate in the form of magnesium ammonium phosphate (struvite) precipitates. When pH of the wastewater was adjusted to 1.2, the removal efficiencies for COD, volatile phenol and sulfide reached 70%, 99% and 100%, respectively. During the second step of precipitation, up to 94% of ammonium was removed from the aqueous phase, and precipitated in the form of struvite with phosphorus. The struvite crystals showed a needle-like structure. X-ray diffraction and transmission electron microscopy were used to characterize the crystallized products.

  8. Coking coal of Checua Lenguazaque area

    International Nuclear Information System (INIS)

    In this report a summary of the main characteristics of the coal of the area of Checua-Samaca is presented. Using the main works carried out on this area, the most important geologic, physical-chemical, technological and petrographic aspects are compiled that are considered essential to carry out a technical evaluation of these coal and all the analyses they take to conclude that in this area, bituminous coal are presented with very good coking properties, on the other hand, it is demonstrated by the use that is given to the coal extracted by the small existent mining. However, keeping in mind the demands of the international market of the coking coal, it becomes necessary to improve the existent geologic information to be able to make reliable stratigraphic correlations

  9. Mortality in retired coke oven plant workers.

    OpenAIRE

    Chau, N.; Bertrand, J P; Mur, J M; Figueredo, A; Patris, A.; Moulin, J J; Pham, Q T

    1993-01-01

    A previous study on 536 retired coke oven plant workers in Lorraine Collieries (France) reported an excess of deaths from lung cancer (standardised mortality ratio (SMR) = 251) compared with the French male population. Occupational exposures during working life were retraced for each subject, but the number of deaths during the observation period (1963-82) was small, and smoking habits were known only for dead subjects. In 1988, the cohort was re-examined (182 deaths occurred between 1963 and...

  10. BRAND COMMITMENTAS ACOMPONENTOFBRAND EQUITY- ARESEARCH CONCERNING COKE

    OpenAIRE

    Ridvan Karalar; Hakan Kiraci

    2007-01-01

    Brand equity is affected by many factors such as brand commitment, brand awareness, perceived quality and brand association. One of them brand royalty is important component of brand equity. In this research, it was investigated consumers’ brand preferences, brand royalty level and brand commitment factors on brands on coke product placed beverage sector. Asurvey carried out on 500 students at Dumlupinar University Economics and Administrative Sciences Faculty. The participants of this stud...

  11. Characterisation of coking activity during supercritical hydrocarbon pyrolysis

    Energy Technology Data Exchange (ETDEWEB)

    Gascoin, Nicolas; Gillard, Philippe; Bernard, Stephane [Laboratoire Energetique, Explosion, Structure, UPRES-EA 1205, 63, avenue de Lattre de Tassigny, 18020 Bourges Cedex (France); Bouchez, Marc [MBDA France, 8, rue Le Brix, 18000 Bourges (France)

    2008-12-15

    The active cooling of the Supersonic Combustion Ramjet engine, for hypersonic flight purpose, is ensured thanks to fuel, n-dodecane for the present study. The endothermic fuel pyrolysis, starting above 800 K, could generate an unwanted coke formation. Experimental tests up to 1125 K and between 1 MPa and 6 MPa have been performed on the hydrocarbon fuel pyrolysis to evaluate the coking activity. 316L stainless steel, low carbon steel and titanium reactors have been considered. A witness of the coke formation, based on its thermal insulation and pressure loss effects, has been found. A correlation between methane production and coke deposit was found. The coke has been studied with Scanning Electron Microscope (SEM), Energy Dispersion Spectroscopy (EDS), X-ray diffractometer and Fourier Transform Infrared (FTIR) spectroscopy. The porosity, the density and the permeability of the coke have been estimated. (author)

  12. A static approach towards coke collapse modelling in blast furnace

    Energy Technology Data Exchange (ETDEWEB)

    Nag, S.; Basu, S. Yu, A.B.

    2009-10-15

    Burden distribution control in a blast furnace has a close relationship with wind acceptance and gas utilisation. Quantification of radial distribution of ore and coke is important for proper control of blast furnace operation. Charging of metallic burden over a layer of coke causes a portion of the coke layer to get dislodged from its original position, similar to the situation observed when a heavy material is dropped on a bed of lighter particles. This phenomenon, designated 'coke collapse', significantly changes the ore/coke distribution in the radial direction and thus affects the permeability of the furnace shaft. In the present work a mathematical model for quantifying the amount of coke collapse has been proposed on the basis of 'stability of slope theory'. The calculation from this model has been compared with the results from experiments in simplified physical models. Predictions of the mathematical model are in good agreement with experimental results.

  13. Water plasmas for the revalorisation of heavy oils and cokes from petroleum refining.

    Science.gov (United States)

    Hueso, José L; Rico, Víctor J; Cotrino, José; Jiménez-Mateos, J M; González-Elipe, Agustín R

    2009-04-01

    This work investigates the possibility of using plasmas to treat high boiling point and viscous liquids (HBPVL) and cokes resulting as secondary streams from the refining of oil. For their revalorisation, the use of microwave (MW) induced plasmas of water is proposed, as an alternative to more conventional processes (i.e., catalysis, pyrolysis, combustion, etc.). As a main result, this type of energetic cold plasma facilitates the conversion at room temperature of the heavy aromatic oils and cokes into linear hydrocarbons and synthesis gas, commonly defined as syngas (CO + H2 gas mixture). The exposure of the coke to this plasma also facilitates the removal of the sulfur present in the samples and leads to the formation on their surface of a sort of carbon fibers and rods network and new porous structures. Besides, optical emission measurements have provided direct evidence of the intermediates resulting from the fragmentation of the heavy oils and cokes during their exposure to the water plasma. Furthermore, the analysis of the mass spectra patterns suggests a major easiness to break the aromatic bonds mainly contained in the heavy oils. Therefore, an innovative method for the conversion of low value residues from oil-refining processes is addressed. PMID:19452916

  14. Toxicological assessment of green petroleum coke.

    Science.gov (United States)

    McKee, Richard H; Herron, Deborah; Beatty, Patrick; Podhasky, Paula; Hoffman, Gary M; Swigert, James; Lee, Carol; Wong, Diana

    2014-01-01

    Green petroleum coke is primarily inorganic carbon with some entrained volatile hydrocarbon material. As part of the petroleum industry response to the high production volume challenge program, the potential for reproductive effects was assessed in a subchronic toxicity/reproductive toxicity screening test in rats (OECD 421). The repeated-dose portion of the study provided evidence for dust accumulation and inflammatory responses in rats exposed to 100 and 300 mg/m(3) but there were no effects at 30 mg/m(3). In the reproductive toxicity screen, the frequency of successful matings was reduced in the high exposure group (300 mg/m(3)) and was not significantly different from control values but was outside the historical experience of the laboratory. The postnatal observations (external macroscopic examination, body weight, and survival) did not indicate any treatment-related differences. Additional tests conducted to assess the potential hazards to aquatic (fish, invertebrates, and algae) and soil dwelling organisms (earthworms and vascular plants) showed few effects at the maximum loading rates of 1000 mg coke/L in aquatic studies and 1000 mg coke/kg soil in terrestrial studies. The only statistically significant finding was an inhibition of algal growth measured as either biomass or growth rate. PMID:24179031

  15. Characterization of flue gas cleaning residues from European solid waste incinerators: assessment of various Ca-based sorbent processes.

    Science.gov (United States)

    Bodénan, F; Deniard, Ph

    2003-05-01

    For the first time, a set of samples of European flue gas cleaning residues, mainly from the incineration of municipal solid waste (MSW), has undergone a mineralogical study. The residues are the result of the neutralization of acid flue gases by lime, the predominant method adopted in Europe, using dry and semi-dry washing processes. The study protocol combines physico-chemical analytical techniques (XRD, FTIR, DSC/TGA) and global chemical analysis enabling identification of the chemical composition of the main constituents, particularly chlorinated Ca-based phases, as well as establishment of modal distributions of the represented phases, both crystalline and amorphous. The samples are slightly hydrated and values vary for trapped Cl, S and even CO(2). The main crystalline phases are NaCl, KCl, CaSO(4), CaCO(3), Ca(OH)(2) and calcium hydroxychloride CaOHCl. CaOHCl is the main chlorine phase, regardless of the treatment process, filtration mode, and specific surface of the Ca-based sorbent. This phase develops during neutralization of HCl by excess lime present according to the reaction Ca(OH)(2)+HCl-->CaOHCl+H(2)O, to the detriment of a complete yield involving the two lime OH groups with formation of CaCl(2).2H(2)O. In addition, it seems that gas temperatures above 150 degrees C increase competition between lime-based neutralization of HCl, SO(2) acid flue gases and CO(2) trapping, thus reducing washing efficiency. PMID:12597999

  16. Urinary 1-hydroxypyrene concentrations in coke oven workers

    OpenAIRE

    Wu, M T; Mao, I F; Ho, C.K.; Wypij, D; Lu, P. L.; Smith, T. J.; Chen, M. L.; Christiani, D C

    1998-01-01

    OBJECTIVES: To investigate the relation of individual occupational exposure to total particulates benzene soluble fraction (BSF) of ambient air with urinary 1-hydroxypyrene (1-OHP) concentrations among coke oven workers in Taiwan. METHODS: 80 coke oven workers and 50 referents were monitored individually for the BSF of breathing zone air over three consecutive days. Exposures were categorised as high, medium, or low among coke oven workers based on exposure situations. The high exposure...

  17. Evaluation of the technological feasibility, and cost of selected control alternatives necessary to meet the proposed Ohio SO/sub 2/ regulations for industrial boilers and processes. Volume I. Youngstown Sheet and Tube Company, Campbell Works - coke oven gas desulfurization. Final report

    Energy Technology Data Exchange (ETDEWEB)

    Hall, R.R.; Stanley, W.T.; Sahagian, J.

    1976-06-01

    This report presents an evaluation by the GCA Corporation, GCA/Technology Division, of the technological feasibility and cost of complying with the proposed Ohio sulfur dioxide regulation (40 FR 52410, November 10, 1975) at Youngstown Sheet and Tube's Campbell Works. The final USEPA Sulfur Dioxide Strategy for the State of Ohio Technical Support Documents, Vol. I and II, (EPA 905/2-76-002) may be obtained from NTIS. The Campbell Works was an example of a by-product coke oven facility. After collecting necessary site and source specific data by means of a plant visit, the technical feasibility of the vacuum carbonate, Dravo Firma, Carl Still, Sulfiban and Holmes Stretford processes were evaluated. Capital and operating costs are presented for the latter three systems.

  18. 76 FR 77020 - Agency Information Collection Activities; Submission for OMB Review; Comment Request; Coke Oven...

    Science.gov (United States)

    2011-12-09

    ... Information Collection Activities; Submission for OMB Review; Comment Request; Coke Oven Emissions ACTION... Administration (OSHA) sponsored information collection request (ICR) titled, ``Coke Oven Emissions,'' to the...: The purpose of Coke Oven Emissions Standard and its information collection requirements, codified...

  19. Mortality of coke plant workers in The Netherlands.

    OpenAIRE

    Swaen, G M; Slangen, J J; Volovics, A.; Hayes, R B; Scheffers, T; Sturmans, F.

    1991-01-01

    During the production of coke, large quantities of coke oven gas are emitted. People who work on the top or on the sides of coke ovens are exposed to this oven gas, which contains a range of carcinogenic chemicals. To investigate the cancer risks under these work conditions, a retrospective study was undertaken. In total 11,399 former workers were enrolled in the study. Of these, 5639 had worked in the coke plant for at least six months between 1945 and 1969. The other 5740 had worked in anot...

  20. Study of coking on heavy petroleum fractions and on models

    Energy Technology Data Exchange (ETDEWEB)

    Belloir, P.F.

    1989-11-01

    After recalling coke formation, thermal behavior of a petroleum fraction from catalytic craking is examined. Thermal sensitivity of diarylethylenes and influence of additives on reaction mechanisms are studied.

  1. Competitive reactions of organophosphorus radicals on coke surfaces.

    Science.gov (United States)

    Catak, Saron; Hemelsoet, Karen; Hermosilla, Laura; Waroquier, Michel; Van Speybroeck, Veronique

    2011-10-17

    The efficacy of organophosphorus radicals as anticoking agents was subjected to a computational study in which a representative set of radicals derived from industrially relevant organophosphorus additives was used to explore competitive reaction pathways on the graphene-like coke surface formed during thermal cracking. The aim was to investigate the nature of the competing reactions of different organophosphorus radicals on coke surfaces, and elucidate their mode of attack and inhibiting effect on the forming coke layer by use of contemporary computational methods. Density functional calculations on benzene and a larger polyaromatic hydrocarbon, namely, ovalene, showed that organophosphorus radicals have a high propensity to add to the periphery of the coke surface, inhibiting methyl radical induced hydrogen abstraction, which is known to be a key step in coke growth. Low addition barriers reported for a phosphatidyl radical suggest competitive aptitude against coke formation. Moreover, organophosphorus additives bearing aromatic substituents, which were shown to interact with the coke surface through dispersive π-π stacking interactions, are suggested to play a nontrivial role in hindering further stacking among coke surfaces. This may be the underlying rationale behind experimental observation of softer coke in the presence of organophosphorus radicals. The ultimate goal is to provide information that will be useful in building single-event microkinetic models. This study presents pertinent information on potential reactions that could be taken up in these models. PMID:21956815

  2. An installation for the intake of coke and the outlet of gases during unloading of coke furnaces

    Energy Technology Data Exchange (ETDEWEB)

    Marapulets, G.N.; Butko, A.V.; Likhogub, Ye.P.; Nayman, A.M.; Pevnyy, V.P.; Yatsura, V.A.; Zinchenko, V.I.

    1982-01-01

    An installation is proposed for receiving coke and the outlet of gases during unloading of coke furnaces, which includes a coke directing dolly, a basket with a dust trapping hood attached to it, a gas outlet, telescopic branchpipe, whose fixed part is attached to the upper part of the hood and a collector for outlet of the gas in the device for purification located parallel to the battery of coking furnaces. To increase the reliability and effectiveness of outlet of the gases, the gas outlet branchpipe is installed horizontally and the telescopic branchpipe is connected by means of levers and linkages to the basket of the coke guide dolly. The dust trapping hood is equipped with an additional, horizontal, gas outlet branchpipe and the gas outlet branchpipes are installed at a distance equal to the distance between the coking furnaces.

  3. Full scale treatment of phenolic coke coking waste water under unsteady conditions

    Energy Technology Data Exchange (ETDEWEB)

    Suschka, Jan [Institute for Ecology of Industrial Areas, Katowice (Poland); Morel, Jacek; Mierzwinski, Stanislaw; Januszek, Ryszard [Coke Plant Przyjazn, Dabrowa Gornicza (Poland)

    1993-12-31

    Phenolic waste water from the largest coke coking plant in Poland is treated at a full technical scale. From the very beginning it became evident that very high qualitative variations in short and long periods were to be expected. For this purpose, the biological treatment plant based on activated sludge is protected through preliminary physical-chemical treatment and the results are secured by a final chemical stage of treatment. Nevertheless, improvements in the performance of the treatment plant have been found necessary to introduce. In this work, the experience gained over the last five years is described and developed improvements were presented. 3 refs., 9 figs., 1 tab.

  4. A novel approach to mitigating sulphur dioxide emissions and producing a mercury sorbent material using oil-sands fluid coke

    International Nuclear Information System (INIS)

    Pyrometallurgical smelting operations are a major source of sulphur dioxide (SO2) which is a precursor to acid rain and increased levels of UV-B penetration in boreal lakes. Mercury is also released in copper smelter off-gas, which can bioaccumulate and cause neurological disorders and death in humans. Fluid coke is produced in massive quantities as a by-product of bitumen upgrading at Syncrude Canada's facility in Fort McMurray, Alberta. Oilsands fluid coke can be used to reduce SO2 and produce elemental sulphur as a co-product. This process was dubbed SOactive. The reaction physically activates the fluid coke to produce a sulphur-impregnated activated carbon (SIAC) which is known as ECOcarbon. Some studies have indicated that SIAC is well suited for the removal of vapour phase mercury, mainly due to the formation of stable mercuric sulphide species. This paper discussed the findings made to date in relation to the SOactive process and the characterization of ECOcarbons. The paper discussed the use of fluid coke for reducing SO2 emissions while producing elemental sulphur as well as coke-SO2-oxygen (O2) and coke-SO2-water (H2O) systems. The paper also examined the production of SIAC products for use in capturing vapour phase mercury. The paper presented the materials and methodology, including an illustration of the apparatus used in reduction of SO2 and activation of fluid coke. It was concluded that more work is still needed to analyse the effect of O2 and SO2 reduction and SIAC properties under smelter flue gas conditions. 10 refs., 1 tab., 8 figs

  5. Treated results study on organic substance and ammonia from coke plant wastewater by SBR method in different operating mode and aeration time conditions

    Institute of Scientific and Technical Information of China (English)

    CHENG Jian-guang; CHEN ping

    2006-01-01

    In this paper, a research was made on the treatment of distillation ammonia wastewater from Tai'an Coke-Plant by SBR(sequencing batch reactors). The feasibility and cost effectiveness was tested. Performance of SBR process treating organic substance and ammonia was presented for different operating pattern and aeration time. The mechanism of the simultaneous nitrification and denitrification from coke plant were analysed on SBR process.

  6. CALDERON COKEMAKING PROCESS/DEMONSTRATION PROJECT

    International Nuclear Information System (INIS)

    This project deals with the demonstration of a coking process using proprietary technology of Calderon, with the following objectives geared to facilitate commercialization: (1) making coke of such quality as to be suitable for use in hard-driving, large blast furnaces; (2) providing proof that such process is continuous and environmentally closed to prevent emissions; (3) demonstrating that high-coking-pressure (non-traditional) coal blends which cannot be safely charged into conventional by-product coke ovens can be used in the Calderon process; and (4) demonstrating that coke can be produced economically, at a level competitive with coke imports. The activities of the past quarter were focused on the following: Conducting bench-scale tests to produce coke and acceptable tar from the process to satisfy Koppers, a prospective stakeholder; Consolidation of the project team players to execute the full size commercial cokemaking reactor demonstration; and Progress made in advancing the design of the full size commercial cokemaking reactor

  7. Kress indirect dry cooling system, Bethlehem Steel's Coke Plant demonstration at Sparrows Point, Maryland. Volume 2. Appendices G-N. Final report, February 1990-February 1992

    International Nuclear Information System (INIS)

    The report provides an evaluation of the Kress Indirect Dry Cooling (KIDC) process. The KIDC process is an innovative system for the handling and cooling of coke produced from a slot type by-product coke oven battery. The report is based on the test work and demonstration of the system at Bethlehem Steel Corporation's Sparrows Point facility in 1991. The report covers both environmental and operational impacts of the KIDC process. The report, Volume 2, contains appendices G-N. Volume 1, PB93-191302, contains the technical report as well as appendices A-F. Volume 2 contains appendixes on coke quality data, blast furnace balwax model report, KIDC operating cost and maintenance requirements, Kress box thickness readings, KIDC coke discharge temperature, QA/QC program, door leak data, and coal data

  8. Clean coal technologies

    International Nuclear Information System (INIS)

    According to the World Energy Council (WEC), at the beginning of the next century three main energy sources - coal, nuclear power and oil will have equal share in the world's total energy supply. This forecast is also valid for the USSR which possesses more than 40% of the world's coal resources and continuously increases its coal production (more than 700 million tons of coal are processed annually in the USSR). The stringent environmental regulations, coupled with the tendency to increase the use of coal are the reasons for developing different concepts for clean coal utilization. In this paper, the potential efficiency and environmental performance of different clean coal production cycles are considered, including technologies for coal clean-up at the pre-combustion stage, advanced clean combustion methods and flue gas cleaning systems. Integrated systems, such as combined gas-steam cycle and the pressurized fluidized bed boiler combined cycle, are also discussed. The Soviet National R and D program is studying new methods for coal utilization with high environmental performance. In this context, some basic research activities in the field of clean coal technology in the USSR are considered. Development of an efficient vortex combustor, a pressurized fluidized bed gasifier, advanced gas cleaning methods based on E-beam irradiation and plasma discharge, as well as new catalytic system, are are presented. In addition, implementation of technological innovations for retrofitting and re powering of existing power plants is discussed. (author)

  9. 基于多属性性能评估的焦炉加热燃烧过程在线优化控制方法%An on-line optimal control method for combustion process of coke oven based on multi-attribute performance evaluation

    Institute of Scientific and Technical Information of China (English)

    雷琪; 颜慧; 吴敏

    2015-01-01

    An on-line optimal control method based on multi-attribute performance evaluation aiming at adjusting the parameters of controllers to suppress the violent fluctuations of the flue temperature in combustion process of coke ovens is proposed, which are caused by the changes of coking time, the fluctuating calories of fuel gas and other factors. Firstly, the coke process characteristics and production demands are analyzed, and a multi-attribute performance evaluation model based on information entropy is proposed to evaluate the performance of the control system on line due to large difference in parameter periods. When the performance of the control system is unsatisfied, however, a multi-objective optimization model is established to minimize the setting time, the deviation and the deviation change of flue temperature. Then, the optimum parameters of the controller are solved by the multi-objective differential evolution algorithm. Finally, simulation results verify that this optimal control method can suppress the fluctuations of flue temperature when the calories of fuel gas and coking time are changing.%针对焦炉加热燃烧过程中控制器参数难以适应由加热煤气热值和结焦时间变化等因素引起的火道温度波动的问题,设计了一种基于多属性性能评估的焦炉加热燃烧过程优化控制方法。首先通过分析焦炉加热燃烧过程的工艺特点及生产需求,针对过程参数周期差异较大的特点,提出了基于信息熵的多属性性能评估模型,实现控制系统的在线性能评估。针对控制系统性能评估不合格的情况,建立了以火道温度偏差、偏差变化率和调节时间为目标的多目标优化模型,并采用差分进化算法进行求解,通过控制器参数的在线调节,保证焦炉火道温度的稳定。仿真结果表明该优化控制方法在加热煤气热值和结焦时间变化时能较好地抑制火道温度的波动。

  10. Effect of Extracted Compositions of Liquefaction Residue on the Structure and Properties of the Formed-coke

    Directory of Open Access Journals (Sweden)

    Song Yong-hui

    2016-01-01

    Full Text Available The purpose of this paper is to study the effect of extracted compositions of the de-ash liquefaction residue (D-DCLR on pyrolysis products yields, compressive strength and composition of the formed-coke, which was prepared by co-pyrolysis of the low metamorphic pulverized coal and D-DCLR. The scanning electron microscope (SEM and the Fourier Transform Infrared (FT-IR were used to characterize the morphology and functional group of the formed-coke, respectively. The results showed that the extracted compositions of D-DCLR were heavy oil (HS, asphaltene (A, pre-asphaltene (PA and tetrahydrofuran isolusion (THFIS, whose contents were 5.10%, 40.90%, 14.4%, 39.60%, respectively. During the pyrolysis process, HS was the main source of tar, and HS, A as well as PA were conducive to improve gas yields. The THFIS helped to improve the yield of the formed-coke up to 89.5%, corresponding to the compressive strength was only 147.7N/ball for the coke. A and PA were the key factors affecting the compressive strength and surface structure of the formed-coke. The compressive strength of coke could be up to 728.0N/ball with adding D-DCLR, which reduced by 50% after the removal of A and PA. The FT-IR analysis showed that the types of surface functional groups of the formed-coke were remained the same after co-pyrolysis, but the absorption peak intensity of each functional group was changed.

  11. Quantification of the Existence Ratio of Non-Adhesion Grain Boundaries and Factors Governing the Strength of Coke Containing Low-Quality Coal

    Science.gov (United States)

    Kanai, Tetsuya; Yamazaki, Yoshiaki; Zhang, Xiaoqing; Uchida, Ataru; Saito, Yasuhiro; Shoji, Masakazu; Aoki, Hideyuki; Nomura, Seiji; Kubota, Yukihiro; Hayashizaki, Hideyuki; Miyashita, Shigeto

    “Non-adhesion grain boundaries” are formed when low-quality coal grains do not adhere to other grains in the carbonization process because of the low dilation of coke. To better understand the effects of non-adhesion grain boundaries on coke strength, the relationship between the existence ratio of non-adhesion grain boundaries and coke strength was investigated quantitatively. The existence ratio of non-adhesion grain boundaries were measured quantitatively by observing the fracture cross-section of coke using scanning electron microscopy (SEM). Coke strength was measured with a diametral-compression test and an I-shape drum index test. As a result, non-adhesion grain boundaries increased with an increase in the blending ratio of low-quality coal. In particular, non-adhesion grain boundaries increased rapidly when the blending ratio of low-quality coal was over 50%. When the ratio was less than 50%, low-quality coals adhered to other caking coal. However, not many low-quality coals adhered to other caking coals when the ratio was over 50%. The tensile strength of coke was not affected by the porosity of coke. However, the tensile strength and the drum index were affected by the existence ratio of non-adhesion grain boundaries. Tensile strength decreased rapidly even for a few non-adhesion grain boundaries because significant defects caused a fracture in the diametral-compression test. However, the I-shape drum index decreased linearly with the existence ratio of the non-adhesion grain boundaries because many fractures occurred during 600 rotations in the drum. The strength of coke containing low-quality coal is governed by the existence ratio of non-adhesion grain boundaries rather than mean values such as the porosity of coke.

  12. Self-cleaning Metal Organic Framework (MOF) based ultra filtration membranes - A solution to bio-fouling in membrane separation processes

    OpenAIRE

    Prince, J. A.; Bhuvana, S.; Anbharasi, V.; Ayyanar, N.; Boodhoo, K. V. K.; Singh, G.

    2014-01-01

    Bio-fouling is a serious problem in many membrane-based separation processes for water and wastewater treatment. Current state of the art methods to overcome this are to modify the membranes with either hydrophilic additives or with an antibacterial compound. In this study, we propose and practise a novel concept to prevent bio-fouling by developing a killing and self-cleaning membrane surface incorporating antibacterial silver nanoparticles and highly hydrophilic negatively charged carboxyli...

  13. Structural variations and physical properties of lignin coke

    International Nuclear Information System (INIS)

    The studied lignin is a by-product of the process of ethanol production from eucaliptus. It was heat-treated under inert atmosphere conditions at increasing temperatures from 3000C up to 26000C. This material has about 35 weight % of carbon yield and low ash content (0.70 w %). The structural variations were studied by wide-angle X-ray diffraction, small-angle X-ray scattering and infra-red spectroscopy. The bulk and the ''real'' density of the samples have also been determined as a function of the heat treatment temperatures. These experimental results enabled us to establish a mechanism of structure variation based on the formation of a graphite-like and porous structure within the initially amorphous lignin matrix. It has been possible to specify the adequate heat treatment temperature based upon the lignin coke applications. (author)

  14. DTA and TGA study of MeSo4 (Me = Fe, Co, Ni dissociation in the presence of coke

    Directory of Open Access Journals (Sweden)

    Boyanov B.S.

    2002-01-01

    Full Text Available MeSO4 (Me = Fe, Co, Ni dissociation is investigated in order to estimate the effect of temperature, time and presence of coke as reducer on the degree and mechanism of dissociation. It is proved that the presence of coke decreases the dissociation temperature considerably and increases the degree of MeSO4 dissociation. Based on the obtained experimental data, a mechanism of the processes is proposed. The obtained results can be used in the industrial production of non-ferrous metals for explaining the processes that take place in the reduction of zinc and lead cakes in order to achieve favorable environmental, technical and economic results.

  15. Effects of operating conditions on compositional characteristics and reaction kinetics of liquid derived by delayed coking of nigerian petroleum residue

    OpenAIRE

    Bello, O. O.; B. T. Ademodi; Macaulay, S. R. A.; G. K. Latinwo

    2006-01-01

    The thermal upgrading of Nigerian petroleum residue was studied at relatively low pressure in a delayed coking reactor system. In this work, the intent was to investigate the effects of process variables such as reaction temperature (200(0)C to 600(0)C), reaction time (0 to 120min), additive concentration loading and additive-to-residue ratio on the amounts and quality of organic liquid product (OLP). The liquid products derived from the delayed coking process were characterized by means of i...

  16. Linhuan Coke oven Cleaner Production 6m Comprehensiv%临涣焦化6m焦炉清洁生产的综合治理

    Institute of Scientific and Technical Information of China (English)

    李峰

    2011-01-01

    The company adopts the new type JN60 6 m coke oven,the production task more nervous,smoke control in the production of absence of difficulty is large.According to the coke oven cleaner production requirements,the company put forward for clean,coking coal "smoke-free,purification tasteless",establishing comprehensive environmental protection to the new concept.First through the search the problems that exist,according to establish management plan,problems with close the technical innovation,to adjust,and the comprehensive management measures,coke oven management to a large volume of coke oven secondary standard.%我公司采用新型JN60型6 m焦炉,生产任务比较紧张,生产中的烟尘逸散控制难度较大。根据焦炉清洁生产要求,公司提出了"备煤无尘、炼焦无烟、净化无味",创建全方位环保新概念。首先通过查找存在的问题,根据问题确立治理方案,装满拉平、技改创新、以调代修等措施综合治理,焦炉管理达到大容积焦炉二级标准。

  17. 29 CFR 1926.1129 - Coke oven emissions.

    Science.gov (United States)

    2010-07-01

    ... 29 Labor 8 2010-07-01 2010-07-01 false Coke oven emissions. 1926.1129 Section 1926.1129 Labor... (CONTINUED) SAFETY AND HEALTH REGULATIONS FOR CONSTRUCTION Toxic and Hazardous Substances § 1926.1129 Coke oven emissions. Note: The requirements applicable to construction work under this section are...

  18. Combustion kinetics of the coke on deactivated dehydrogenation catalysts

    NARCIS (Netherlands)

    Luo, Sha; He, Songbo; Li, XianRu; Li, Jingqiu; Bi, Wenjun; Sun, Chenglin

    2015-01-01

    The coke combustion kinetics on the deactivated catalysts for long chain paraffin dehydrogenation was studied by the thermogravimetry and differential thermogravimetry (TG–DTG) technique. The amount and H/C mole ratio of the coke were determined by the TG and elemental analysis. And the comprehensiv

  19. CARCINOGEN ASSESSMENT OF COKE OVEN EMISSIONS (REVISED DRAFT)

    Science.gov (United States)

    Coke oven workers in Allegheny County, Pennsylvania and at 10 non-Allegheny County coke plants in the United States and Canada were found to be at an excess risk of mortality from cancer of all sites and from cancer of the lungs, bronchus, and trachea, kidney, and prostate. An im...

  20. Carbon Tubular Morphologies in Blast Furnace Coke

    OpenAIRE

    Stanislav S. Gornostayev; Jouko J. Härkki

    2008-01-01

    The paper reports on the first occurrence of microscale carbon tubular morphologies (CMTs) in a blast furnace (BF) coke. The CMTs were probably formed as a result of the conversion of solid disordered carbon via liquid phase metal particles involving a gas phase containing a substantial amount of N 2 and O 2 . The presence of CMTs may lie behind the generation of the smallest fraction of fines in BF exhaust dust. If the amount of CMTs present in the BF exhausts gases at any particular metallu...

  1. Carbon Tubular Morphologies in Blast Furnace Coke

    Directory of Open Access Journals (Sweden)

    Stanislav S. Gornostayev

    2008-01-01

    Full Text Available The paper reports on the first occurrence of microscale carbon tubular morphologies (CMTs in a blast furnace (BF coke. The CMTs were probably formed as a result of the conversion of solid disordered carbon via liquid phase metal particles involving a gas phase containing a substantial amount of N2 and O2. The presence of CMTs may lie behind the generation of the smallest fraction of fines in BF exhaust dust. If the amount of CMTs present in the BF exhausts gases at any particular metallurgical site proves to be substantial, it could become a subject of environmental concern.

  2. Clean catch urine sample

    Science.gov (United States)

    Urine culture - clean catch; Urinalysis - clean catch; Clean catch urine specimen; Urine collection - clean catch ... lips" (labia). You may be given a special clean-catch kit that contains sterile wipes. Sit on ...

  3. A Real-Time Mathematical Model for the Two-Dimensional Temperature Field of Petroleum Coke Calcination in Vertical Shaft Calciner

    Science.gov (United States)

    Xiao, Jin; Huang, Jindi; Zhong, Qifan; Li, Fachuang; Zhang, Hongliang; Li, Jie

    2016-02-01

    A real-time mathematical model for the two-dimensional temperature field of petroleum coke calcination in vertical shaft calciner was developed based on computational fluid dynamics. In the modeling process, the petroleum coke discharging process was described by the solid viscous flow, the dynamic heat flux boundary condition was adopted to specify the heat transfer between the flue wall and the gas in the flue, and the Arrhenius equation was used to characterize the pyrolysis process of petroleum coke. The model was validated with both measurement data and data from the literature. The effects of discharge rate per pot, volatile content of green coke, and excess air coefficient on the temperature field of the vertical shaft calciner were investigated with the use of the developed model. The following reasonable operating conditions were obtained: the discharge rate per pot should be less than 90 kg/h, the volatile content of green coke should be in the range of 9-11%, and the excess air coefficient should be in the range of 1.10-1.20. In this work, the governing equations were discretized by using the finite volume method, and the discrete linear equations were solved by using sparse matrix package UMFPACK. The model calculating process takes about less than 15 s. Therefore, the model is beneficial in realizing real-time online temperature detection of petroleum coke calcination in a vertical shaft calciner.

  4. Coke deactivation of catalysts for hydroprocessing of heavy petroleum feedstocks

    International Nuclear Information System (INIS)

    Harwell's principal contribution to the study of the role of coke in the deactivation of catalysts for hydroprocessing of heavy petroleum feedstocks has been the development and application of nuclear microprobe methods to measure the distributions of hydrogen, carbon, nitrogen and other elements in coked catalyst pellets. Nuclear microprobe methods have been developed that allow the measurement of the distribution of carbon, hydrogen, nitrogen and heavier elements in coked catalyst pellets. At present analysis by both deuteron and helium-4 ion beams is necessary to cover the complete range of elements. The potential of using helium-3 irradiation alone to measure all elements is as yet unrealised. Applications have included studies of the variability of profiles in batches of used pellets, investigation of interrelationships between coke components and limited kinetic studies. Many of these applications have proved to be successful and nuclear microprobe methods should continue to be exploited studies of catalyst coking. (au)

  5. Effect of physical disturbance on the structure of needle coke

    Science.gov (United States)

    Zhao, Shi-Gui; Wang, Bao-Cheng; Sun, Quan

    2010-10-01

    Through different preparation technology, this paper reports that the needle coke is prepared with coal-tar pitch under the effect of magnetic field and ultrasonic cavitation. It studies the effect of physical disturbance on the structure of needle coke. The structure of needle coke is characterized by scanning electron microscope and x-ray diffractometer, and the influence mechanism is analysed. Results showed that the structure and property of needle coke could be effectively improved by magnetic field and ultrasonic cavitations, such as degree of order, degree of graphitization and crystallization. Comparatively speaking, the effect of magnetic field was greater. The graphitization degree of needle coke prepared under the effect of magnetic field is up to 45.35%.

  6. On Dust Removing of Coke Oven's Charging and Discharging%焦炉装煤出焦联合除尘述评

    Institute of Scientific and Technical Information of China (English)

    王恭铎

    2000-01-01

    介绍了几种国内外焦炉装煤出焦联合除尘系统,对其进行了评述,并提出在实施过程中可采用系统的建议。%Several dust removing systems of coke oven's coal charging and coke discharging process both at home and abroad are introduced and reviewed, and suggestions for optimum system in practical application are proposed.

  7. Mid and long term behaviour in soils of pollutants from coke pyrolysis process; Comportement a moyen et long terme dans le sous-sol de polluants issus du processus de pyrolyse de la houille

    Energy Technology Data Exchange (ETDEWEB)

    Bonnet, F.

    1998-07-01

    Nowadays, the industrialists have to take into account the potential pollution on their exploitation sites. In order to better understand the soils-pollutants interaction mechanisms, have been observed: (1)the de-pollution of a soil, (2)the retention capacity of a soil for pollutants contained in aqueous solution, (3)the migration of pollutants in a soil. A methodology study of the repartition of the hydrocarbon pollution in a soil is proposed. It uses easy means and leads to the pollutants characterization in soils (global charge of pollution and granulometric distribution). The agglomeration state of grains and the middle size of agglomerates seem to be the main parameters to understand the dissolution and transfer of pollutants in environment. Waters are one of the main vector of diffusion of the pollution. Tests of water percolation have been carried out. As a matter of fact, pollution due to coke pyrolysis (essentially polycyclic aromatic hydrocarbons: PAHs), is relatively stable. Indeed, the percentage of leached PAHs is rarely above 1% (for a soil containing about 400 mg of PAH per kg of soil). Sometimes, under some conditions it can be more dangerous to cleanse a polluted soil than to leave it in its place (on account of the release of the pollutants). The first element which can retain the pollutants and prevent their diffusion is the soil. Whatever is the pollutant studied in solution (NH{sub 4}{sup +}, phenol or naphthalene), there is interaction between the soil and each pollutant. Nevertheless, the retention capacity of a soil depends of the pollutant and of the nature of the soil. According to the soil considered, the retention of a pollutant can vary between 1 to 10. On account of a composition which is often heterogeneous for soils of industrial sites, the difficulty will be to predict the conditions in which the polluted solutions will circulate. (O.M.)

  8. Study of the petroleum schedules thermal cleaning process from asphalt, ressin and paraffin deposits using low- temperature plasma

    Science.gov (United States)

    Samigullin, A. D.; Galiakbarov, A. T.; Galiakbarov, R. T.

    2016-01-01

    Petroleum industry uses large amount of pumping and compression pipes. Carrying out the whole range of repair works requires cleaning of the pipe inner surface from deposits which appeared in it during operation [1]. The task of asphalt, resin and paraffin deposits control remains one of the most essential for the branch. The article deals with thermal method and device for asphalt, resin and paraffin deposits removal from pumping and compression pipes inner surface, describes and provides the device application scope for cleaning the pumping and compression pipes inner surface. To deal with borehole equipment and pipe systems waxing problem various deposit prevention and removal methods are used, including mechanical, thermal, chemical, combined and nonconventional methods.

  9. Coke: Capacity Expansion and Production Closure / Restriction Go Side by Side

    Institute of Scientific and Technical Information of China (English)

    2007-01-01

    @@ With the "self production restriction" and the "closure of small coking enterprises" in the coking sector and the rapid demand increase in downstream metallurgical and chemical sectors, a basic supply/demand balance of coke was achieved in 2006 and the price of coke also made a gradual pickup from the second quarter of 2007.

  10. Effect of nut coke on the performance of the ironmaking blast furnace

    NARCIS (Netherlands)

    Song, Q.

    2013-01-01

    The blast furnace consumes a large amount of high quality metallurgy coke (size 35-80 mm) in addition to ore in the form of pellets and sinter. This coke is the coarse fraction, derived from the coke plant. The fine fraction (8 -35 mm), arise after sieving, named nut coke, can’t be directly used in

  11. Design and operation of the coke-oven gas sulfur removal facility at Geneva Steel

    Energy Technology Data Exchange (ETDEWEB)

    Havili, M.U.; Fraser-Smyth, L.L.; Wood, B.W. [Geneva Steel, Provo, UT (United States)

    1996-02-01

    The coke-oven gas sulfur removal facility at Geneva Steel utilizes a combination of two technologies which had never been used together. These two technologies had proven effective separately and now in combination. However, it brought unique operational considerations which has never been considered previously. The front end of the facility is a Sulfiban process. This monoethanolamine (MEA) process effectively absorbs hydrogen sulfide and other acid gases from coke-oven gas. The final step in sulfur removal uses a Lo-Cat II. The Lo-Cat process absorbs and subsequently oxidizes H{sub 2}S to elemental sulfur. These two processes have been effective in reducing sulfur dioxide emissions from coke-oven gas by 95%. Since the end of the start-up and optimization phase, emission rate has stayed below the 104.5 lb/hr limit of equivalent SO{sub 2} (based on a 24-hr average). In Jan. 1995, the emission rate from the sulfur removal facility averaged 86.7 lb/hr with less than 20 lb/hr from the Econobator exhaust. The challenges yet to be met are decreasing the operating expenses of the sulfur removal facility, notably chemical costs, and minimizing the impact of the heating system on unit reliability.

  12. Reducibility study of Rossetta ilmenite ore briquettes and powder with coke breeze at 800-1100°C

    Directory of Open Access Journals (Sweden)

    Abd el Gawad Hala H.

    2013-01-01

    Full Text Available Ilmenite ore fine and coke breeze as reduced material were briquetted with different amounts of organic materials such as molasses or pitch were studied in this investigation. The produced briquettes at reasonable condition were reduced in nitrogen atmosphere at temperature range 800 - 1100oC to determine the factors controlling the reduction and to determine the controlling mechanism. Also ilmenite ore fine with coke breeze were reduced at the same temperature range in nitrogen atmosphere without briquetting process, for the sake of comparison.

  13. Comparative investigations of zeolite catalyst deactivation by coking in the conversion of methanol to hydrocarbons

    OpenAIRE

    Evensen, Kjetil Gurholt

    2014-01-01

    With large countries as India and China in tremendous development accompanied by a growing worldwide population, questions arise in how energy demands can be met in the post-oil society. The methanol-to-hydrocarbon process, catalysed by Brønsted acidic zeolites, constitutes an alternative route for the production of gasoline and other valuable hydrocarbons from feedstocks such as natural gas and coal. Catalyst deactivation by coke formation is nevertheless a big concern, and a better understa...

  14. Choosing a coke-oven gas desulfurization system: a review of current technology

    Energy Technology Data Exchange (ETDEWEB)

    Lynch, P.A.

    1982-12-01

    Installation of coke-oven gas desulphurizing systems is primarily the result of air pollution control regulations. Although not currently profitable, operating costs can be minimized by choosing the technology most suited to the particular application. The Stretford Holmes, Takahax/Hirohax, Koppers Vacuum Carbonate, Sulfiban and Dravo/Still processes are discussed, together with criteria for economic analysis based on technical and by-product market evaluations.

  15. Equilibrium prediction of CO2 reforming of coke oven gas: Suitability for methanol production

    OpenAIRE

    Bermúdez Menéndez, José Miguel; Arenillas de la Puente, Ana; Menéndez Díaz, José Ángel

    2012-01-01

    [EN] A thermodynamic study of the equilibrium of the CO2 reforming of coke oven gas (COG) was carried out with the aid of Aspen Plus® software. The influence of various operation conditions (temperature, pressure, COG composition and CO2/CH4 ratio) upon different parameters (conversions, yields, outlet composition, carbon production, by-products) was studied in order to evaluate the suitability of the process for producing a synthesis gas appropriate for methanol production. It was establishe...

  16. Dynamics study on effect of temperature to Nitrous nitrification reaction of coking wastewater

    Institute of Scientific and Technical Information of China (English)

    SHAN Ming-jun; ZHANG Hai-ling; LU Yan-li

    2007-01-01

    Dynamic effects of NO2 - - N accumulation were discussed owing to temperature. In different temperature, a series ofvmax and Ks were found considering the relation between the temperature and rate of ammonia nitrogen transforming into NO2 - - N. The kinetics models, which reflected the conditions of ammonia nitrogen transforming into NO2 - - N in the treatment process of the coking wastewater, were built up. The characteristic coefficient temperature was determined according to Arrhenius.

  17. Lessons learned from a rigorous peer-review process for building the Climate Literacy and Energy Awareness (CLEAN) collection of high-quality digital teaching materials

    Science.gov (United States)

    Gold, A. U.; Ledley, T. S.; McCaffrey, M. S.; Buhr, S. M.; Manduca, C. A.; Niepold, F.; Fox, S.; Howell, C. D.; Lynds, S. E.

    2010-12-01

    The topic of climate change permeates all aspects of our society: the news, household debates, scientific conferences, etc. To provide students with accurate information about climate science and energy awareness, educators require scientifically and pedagogically robust teaching materials. To address this need, the NSF-funded Climate Literacy & Energy Awareness Network (CLEAN) Pathway has assembled a new peer-reviewed digital collection as part of the National Science Digital Library (NSDL) featuring teaching materials centered on climate and energy science for grades 6 through 16. The scope and framework of the collection is defined by the Essential Principles of Climate Science (CCSP 2009) and a set of energy awareness principles developed in the project. The collection provides trustworthy teaching materials on these socially relevant topics and prepares students to become responsible decision-makers. While a peer-review process is desirable for curriculum developer as well as collection builder to ensure quality, its implementation is non-trivial. We have designed a rigorous and transparent peer-review process for the CLEAN collection, and our experiences provide general guidelines that can be used to judge the quality of digital teaching materials across disciplines. Our multi-stage review process ensures that only resources with teaching goals relevant to developing climate literacy and energy awareness are considered. Each relevant resource is reviewed by two individuals to assess the i) scientific accuracy, ii) pedagogic effectiveness, and iii) usability/technical quality. A science review by an expert ensures the scientific quality and accuracy. Resources that pass all review steps are forwarded to a review panel of educators and scientists who make a final decision regarding inclusion of the materials in the CLEAN collection. Results from the first panel review show that about 20% (~100) of the resources that were initially considered for inclusion

  18. Study and Application of Sealing Material for Coke Oven Chamber

    Institute of Scientific and Technical Information of China (English)

    GAN Feifang; TAI Li

    2005-01-01

    A kind of dry refractory sealing material has been developed to repair the fine cracks in coke oven chamber. With silica sand as the main raw material, the sealing material is blown into coke oven chamber by compressed air while being applied, and bonded to brick surface or filled in fine cracks of chamber under right pressure. The physical properties of the material are similar to those of silica bricks during its application. So it can be adapted to conditions of coke oven and has good service life. The study and application results of the sealing material are described in this paper.

  19. THE INERT HOLDING RATIO OF COAL ANDTHE STRENGTH OF COKE

    Institute of Scientific and Technical Information of China (English)

    陈鹏

    1996-01-01

    The variation regularity of coke strength was investigated in terms of the genetic fac-tors and petrographic parameters of coal in collaboration with the technical properties of coal. Aconcept of inert holding ratio of coal was proposed. There is an optimal inert holding ratio for dif-ferent ranks of coals for making coke with highest combined strength. The additive property of in-ert holding ratio under normal conditions was demonstrated with actual examples of coal blending.Thus it is possible to predict the combined strength of coke through reflectance, content of inertcomponents and caking index (Ro, max-I-G) diagram system.

  20. Characteristics of laboratory-coked resid HDS catalyst

    Energy Technology Data Exchange (ETDEWEB)

    Baumgart, J. Wang, Y.; Ernst, W.R. (Georgia Inst. of Tech., Atlanta (USA))

    1990-12-01

    A sample of commercial residual oil hydrotreating catalyst with a bimodal pore structure was coked to progressively higher levels with styrene at 425{degree}C. Measurements of porosity by mercury intrusion-extrusion porosimetry, nitrogen adsorption-desorption porosimetry, and coronene diffusivity reveal the importance of the pore network to the structure of the coked catalyst. The role played by 'shielded' large pores within the structure is demonstrated. It is proposed that coking first occurs at the junctions between large, shielded pores and narrow connecting pores. The results are discussed in terms of the theoretical predictions of Mann and co-workers.

  1. The construction of a process line for high efficiency silicon solar cells under clean-room conditions

    International Nuclear Information System (INIS)

    The aim of this research project was to plan, construct and test a clean-room technology laboratory for the manufacturing of silicon solar cells with 20% efficiency (1.5AM). In addition to the establishment of the laboratory, there existed the case of establishing the material and technological fundamentals of high-efficiency solar cells, testing and optimizing all stages of production as well as constructing test stands for accompanying characterisation work. The following final report describes the construction of the laboratory and characterisation systems, the material elements of high-efficiency solar cells as well as the most important results of solar cell production and optimisation. (orig./BWI)

  2. TGA and DMA studies of blends from very good coking Zofiowka coal and various carbon additives: Weakly coking coals, industrial coke and carbonized plants

    Energy Technology Data Exchange (ETDEWEB)

    Krzesinska, M. [Centre of Polymer and Carbon Materials, Polish Academy of Sciences, Marii Curie- Sklodowskiej 34, PL-41819 Zabrze (Poland); Silesian Technical University, Department of Electron Technology, Institute of Physics, Krzywoustego 2, PL-44100 Gliwice (Poland); Szeluga, U.; Majewska, J.; Pusz, S.; Czajkowska, S. [Centre of Polymer and Carbon Materials, Polish Academy of Sciences, Marii Curie- Sklodowskiej 34, PL-41819 Zabrze (Poland); Smedowski, L. [Silesian Technical University, Department of Electron Technology, Institute of Physics, Krzywoustego 2, PL-44100 Gliwice (Poland); Kwiecinska, B. [AGH-University of Science and Technology, Aleja Mickiewicza 30, PL-30059 Krakow (Poland)

    2010-04-01

    The aim of this work is to study the effects of various carbon additives, blended with very good coking coal, on the thermal decomposition of the blends. The blends possess fixed content (50 wt.%) of very good coking coal from the Zofiowka Mine. The remaining components of the blends are worse coking coals collected from the Janina, Krupinski, Szczyglowice, Jas-Mos mines (coals of carbon content ranging from 73 up to 92 wt.%), and very porous carbons: coke (from the coking plant Zdzieszowice), as well as woody stems of bamboo and yucca carbonized at 400 C. The content of porous carbon in a blend does not exceed 20 wt.%. Thermogravimetric analysis (TGA) and dynamic mechanical analysis (DMA) are used in the study. The weight loss during low-temperature pyrolysis (< 600 C), and storage/loss elastic moduli measured as a function of the increasing temperature are related to the kind and concentration of additives. The temperature dependences of elastic moduli determined for binary coal blends differ clearly from those of ternary coal blends. The consumption of energy during the interaction of the components in binary blends was found to be distinctly bigger than the one observed for ternary blends. Non-softening additives such as carbonized plants and low rank coal, containing many functional groups, diminish both moduli of the blends distinctly. However, the addition of coke does not reduce the value of the elastic moduli but increases the width of the maximum occurring in the temperature dependence of the moduli. The influence of the coke additive on rheological properties of the blends, different in comparison with the remaining additives studied, was assigned with different number of functional groups and radicals. (author)

  3. Contact cleaning of polymer film solar reflectors

    Science.gov (United States)

    Sansom, Christopher; Fernández-García, Aránzazu; Sutter, Florian; Almond, Heather; King, Peter

    2016-05-01

    This paper describes the accelerated ageing of polymer film reflecting surfaces under the conditions to be found during contact cleaning of Concentrating Solar Power (CSP) collectors in the presence of dust and sand particles. In these situations, contact cleaning using brushes and water is required to clean the reflecting surfaces. Whilst suitable for glass reflectors, this paper discusses the effects of existing cleaning processes on the optical and visual properties of polymer film surfaces, and then describes the development of a more benign but effective contact cleaning process for cleaning polymer reflectors. The effects of a range of cleaning brushes are discussed, with and without the presence of water, in the presence of sand and dust particles from selected representative locations. Reflectance measurements and visual inspection shows that a soft cleaning brush with a small amount of water can clean polymer film reflecting surfaces without inflicting surface damage or reducing specular reflectance.

  4. Thermal degradation of cold cured anthracite/coke breeze briquettes prepared from a coal tar acid resin

    Energy Technology Data Exchange (ETDEWEB)

    Thoms, L.J.; Snape, C.E.; Taylor, D.; Mullens, J.; Mullens, S. [University of Strathclyde, Glasgow (United Kingdom). Department of Pure & Applied Chemistry

    1999-07-01

    Phenolic resoles were synthesised using a coal tar acid fraction of the oil from a low temperature carbonisation process. Anthracite/coke breeze briquettes were prepared using the tar acid resoles. Thermogravimetric analysis-mass spectrometry of products and combustion of briquettes are described. 4 refs., 1 tab.

  5. The total coking plant wastewater, the problem of its treatment and utilization

    Energy Technology Data Exchange (ETDEWEB)

    Vyskrebets, A.M.; Kozenko, L.I.; Nikolaeva, N.A.; Ludyanskii, M.L.

    1982-01-01

    An investigation was made into the characteristics, treatment, and possible uses of the coking plant wastewater. Included were data on the volumes of wastewater from various processes in the coking plants. Also included were data on the contaminants of the various components and the total wastewater. Among other suggestions, it was recommended that all contaminated waters be kept from the storm sewer system. It was concluded that an increase in the coefficients of evaporation and treatment of the water with copper tetraamine sulfate would permit a decrease in the demand for fresh water and a decrease in the discharge from the plant. Also, it was concluded that a major obstacle in the use of the total effluent was mineralization. Seven tables of data were included in the work.

  6. Formation of nitrogen-containing compounds during slow pyrolysis and oxidation of petroleum coke

    Energy Technology Data Exchange (ETDEWEB)

    Furimsky, E.; Ohtsuka, Y. [IMAF Group, Ottawa, ON (Canada)

    1997-09-01

    The petroleum coke from a fluid coking process was pyrolyzed in helium and oxidized in 1% and 4% O{sub 2} and in air, with the aim to determine N-containing compounds such as HCN, NH{sub 3}, NO, and N{sub 2}O. The experiments were performed with and without limestone. NO was the major product during all oxidation runs. N{sub 2}O was formed only in air. In this case, N{sub 2}O formation was delayed when compared with that of NO. The addition of limestone decreased formation of HCN and increased that of NH{sub 3}, whereas NO formation was least affected. 36 refs., 8 figs., 6 tabs.

  7. Development of OTM Syngas Process and Testing of Syngas Derived Ultra-clean Fuels in Diesel Engines and Fuel Cells

    Energy Technology Data Exchange (ETDEWEB)

    E.T. Robinson; John Sirman; Prasad Apte; Xingun Gui; Tytus R. Bulicz; Dan Corgard; John Hemmings

    2005-05-01

    This final report summarizes work accomplished in the Program from January 1, 2001 through December 31, 2004. Most of the key technical objectives for this program were achieved. A breakthrough material system has lead to the development of an OTM (oxygen transport membrane) compact planar reactor design capable of producing either syngas or hydrogen. The planar reactor shows significant advantages in thermal efficiency and a step change reduction in costs compared to either autothermal reforming or steam methane reforming with CO{sub 2} recovery. Syngas derived ultra-clean transportation fuels were tested in the Nuvera fuel cell modular pressurized reactor and in International Truck and Engine single cylinder test engines. The studies compared emission and engine performance of conventional base fuels to various formulations of ultra-clean gasoline or diesel fuels. A proprietary BP oxygenate showed significant advantage in both applications for reducing emissions with minimal impact on performance. In addition, a study to evaluate new fuel formulations for an HCCI engine was completed.

  8. Coke deposition mechanism on the pores of a commercial Pt-Re/{gamma}-Al{sub 2}O{sub 3} naphtha reforming catalyst

    Energy Technology Data Exchange (ETDEWEB)

    Baghalha, Morteza; Mohammadi, Mohammad; Ghorbanpour, Arian [Department of Chemical and Petroleum Engineering, Sharif University of Technology, Azadi St., Tehran, 11365-9465 (Iran)

    2010-07-15

    Coke deposition mechanism on a commercial Pt-Re/{gamma}-Al{sub 2}O{sub 3} naphtha reforming catalyst was studied. A used catalyst that was in industrial reforming operation for 28 months, as well as the fresh catalyst of the unit were characterized using XRD, XRF, and nitrogen adsorption/desorption analyses. Carbon and sulfur contents of the fresh and the used catalysts were determined using Leco combustion analyzer. The pore size distributions (PSD) of the fresh and the used reforming catalysts were determined using BJH and Comparison Plot methods. The Comparison Plot method produced the most reasonable PSDs for the catalysts. Through comparison of the PSDs of the fresh and the used catalysts, it was revealed that coke deposited on both micropores and mesopores of the catalyst at a constant thickness of 1.0 nm. The constant coke thickness on the catalyst pore walls in the naphtha reforming process (temp. {proportional_to} 500 C) implies that coke deposition reaction is the slow controlling step in comparison to the fast mass transfer rate of coke ingredients into the pores. The bulk density of the deposited coke on the used catalyst was calculated as 0.966 g/cm{sup 3}. (author)

  9. Semi-coke briquettes: towards reducing emissions of primary PM2.5, particulate carbon, and carbon monoxide from household coal combustion in China

    Science.gov (United States)

    Li, Qing; Li, Xinghua; Jiang, Jingkun; Duan, Lei; Ge, Su; Zhang, Qi; Deng, Jianguo; Wang, Shuxiao; Hao, Jiming

    2016-01-01

    Direct household use of unprocessed raw coals for cooking and heating without any air pollution control device has caused serious indoor and outdoor environment problems by emitting particulate matter (PM) and gaseous pollutants. This study examined household emission reduction by switching from unprocessed bituminous and anthracite coals to processed semi-coke briquettes. Two typical stoves were used to test emission characteristics when burning 20 raw coal samples commonly used in residential heating activities and 15 semi-coke briquette samples which were made from bituminous coals by industrial carbonization treatment. The carbonization treatment removes volatile compounds from raw coals which are the major precursors for PM formation and carbon emission. The average emission factors of primary PM2.5, elemental carbon, organic carbon, and carbon monoxide for the tested semi-coke briquettes are much lower than those of the tested raw coals. Based on the current coal consumption data in China, switching to semi-coke briquettes can reduce average emission factors of these species by about 92%, 98%, 91%, and 34%, respectively. Additionally, semi-coke briquette has relatively lower price and higher burnout ratio. The replacement of raw coals with semi-coke briquettes is a feasible path to reduce pollution emissions from household activities.

  10. Modeling and Simulation of Petroleum Coke Calcination in Pot Calciner Using Two-Fluid Model

    Science.gov (United States)

    Xiao, Jin; Huang, Jindi; Zhong, Qifan; Zhang, Hongliang; Li, Jie

    2016-02-01

    The aim of this work was to establish a mathematical model for the analysis of calcining process of petroleum coke in a 24-pot calciner via computational fluid dynamics (CFD) numerical simulation method. The model can be divided into two main parts (1) heterogeneous reacting flow of petroleum coke calcination in the pot was simulated using a two-fluid model approach where the gas and solid phase are treated as a continuous phases; and (2) the standard turbulence equations combined with the finite rate/eddy-dissipation combustion model and discrete ordinates model were solved for the turbulent gas reacting flow in the flue. The model of the calcining process was implemented in ANSYS Fluent 15.0 (commercial CFD software) and validated by industrial production data. After the validation research, the model has been applied to inspect the distribution features of the temperature field in the furnace, the concentration field of residual moisture and volatiles in the petroleum coke, and the vector velocity field of gas and solid phases. This research can provide a theoretical basis for optimizing the structure and improving the automatic control level of a pot calciner.

  11. KCCC: Coke and Coal Chemical Business Opens up Growth Space

    Institute of Scientific and Technical Information of China (English)

    2007-01-01

    @@ Kailuan Clean Coal Co., Ltd. (KCCC, SH: 600997) is located in Kailuan, Hebei province. Its main business includes the mining of coal and accompanying resources, the dressing and processing of raw coal, the sales of coal products and the production and sales ofcoking products.

  12. Review On Automatic-Cleaning Basket Strainer

    OpenAIRE

    Deepak Gothwal; Abhijit Dhumal; Anand Gang; Siddharth Gavali; Sandip Shinde

    2015-01-01

    Abstract Clean water is a basic need of every individual. Today in numerous cities of India large number of waste water is produced. Such waste water is polluting natural water bodies like rivers lakes etc. Hence waste water filtration amp waters final purification is need of hour. In conventional type of filters when strainer gets clogged we have to manually clean it which takes time amp filtration processes stops during cleaning process. While in Self-Cleaning Basket Strainer when strainer ...

  13. Changes in the microstructure of coke while passing the blast furnace with respect to the quality of the charged coke and the behaviour of nut coke in the blast furnace

    Energy Technology Data Exchange (ETDEWEB)

    Janhsen, U.; Guenbati, A.; Sautner, C. (and others) [ThyssenKrupp Steel, Duisburg (Germany)

    2007-07-01

    This study provides a comprehensive contribution to the understanding of the metallurgical stresses to which the coke is exposed in a blast furnace. The investigations refer to the change in the coke microstructure depending on the charged feed coke quality and the blast furnace operatic conditions. Also the behaviour of nut coke (coke - 35 mm) in the blast furnace is determined. To work on the scheduled activities and aims of the project various tools are used by the different partners. At TKS, a new microscopic measurement method quantifying the change in the coke carbon micro texture is used to compare the microstructure of feed coke, CRI/CSR treated coke and core drilled coke from the tuyere level of different TKS blast furnaces. Tuyere core drill exercises also are used to detect ZrO{sub 2} traced nut coke charged as mix with burden components in the lower part of the furnace, CSM used the MOSCA model and tuyere core drillings to investigate the behaviour of the nut at a blast furnace of Lucchini at Piombino (Italy). At MEFOS, cokes excavated from LKAB's Experimental Blast Furance (EBF) are used as a basis for the research. The evolution of the EBF coke properties, particuly the carbon structure and alkali uptake were related to CO{sub 2} reactivity. At DMT synthetic coke materials of various qualites are produced for laboratory investigations also at the partner. The University of Aachen RWTH studies the behaviour of coke under various blast furnace scenarios to detect also the changes in the coke microstructure. 12 refs., 141 figs., 63 tabs.

  14. Coke Formation During Hydrocarbons Pyrolysis. Part One: Steam Cracking Formation de coke pendant la pyrolise des hydrocarbures. Première partie : vapocraquage

    OpenAIRE

    Weill J.; Broutin P.; Billaud F.; Gueret C.

    2006-01-01

    Thermal cracking is always accompanied by coke formation, which becomes deposited on the wall and limits heat transfers in the reactor while increasing pressure drops and possibly even plugging up the reactor. This review article covers undesirable coking operations in steam craking reactors. These coking reactions may take place in the gas phase and/or on the surface of the reactor, with coke being produced during pyrolysis by a complex mechanism that breaks down into a catalytic sequence an...

  15. [Health risk assessment of coke oven PAHs emissions].

    Science.gov (United States)

    Bo, Xin; Wang, Gang; Wen, Rou; Zhao, Chun-Li; Wu, Tie; Li, Shi-Bei

    2014-07-01

    Polycyclic aromatic hydrocarbons (PAHs) produced by coke oven are with strong toxicity and carcinogenicity. Taken typical coke oven of iron and steel enterprises as the case study, the dispersion and migration of 13 kinds of PAHs emitted from coke oven were analyzed using AERMOD dispersion model, the carcinogenic and non-carcinogenic risks at the receptors within the modeling domain were evaluated using BREEZE Risk Analyst and the Human Health Risk Assessment Protocol for Hazardous Waste Combustion (HHRAP) was followed, the health risks caused by PAHs emission from coke oven were quantitatively evaluated. The results indicated that attention should be paid to the non-carcinogenic risk of naphthalene emission (the maximum value was 0.97). The carcinogenic risks of each single pollutant were all below 1.0E-06, while the maximum value of total carcinogenic risk was 2.65E-06, which may have some influence on the health of local residents. PMID:25244863

  16. Demonstrating practical application of soil and groundwater clean-up and recovery technologies at natural gas processing facilities: Bioventing, air sparging and wetlands remediation

    International Nuclear Information System (INIS)

    This issue of the project newsletter described the nature of bioventing, air sparging and wetland remediation. It reviewed their effectiveness in remediating hydrocarbon contaminated soil above the groundwater surface. Bioventing was described as an effective, low cost treatment in which air is pumped below ground to stimulate indigenous bacteria. The bacteria then use the oxygen to consume the hydrocarbons, converting them to CO2 and water. Air sparging involves the injection of air below the groundwater surface. As the air rises, hydrocarbons are stripped from the contaminated soil and water. The advantage of air sparging is that it cleans contaminated soil and water from below the groundwater surface. Hydrocarbon contamination of wetlands was described as fairly common. Conventional remediation methods of excavation, trenching, and bellholes to remove contamination often cause extreme harm to the ecosystem. Recent experimental evidence suggests that wetlands may be capable of attenuating contaminated water through natural processes. Four hydrocarbon contaminated wetlands in Alberta are currently under study. Results to date show that peat's high organic content promotes sorption and biodegradation and that some crude oil spills can been resolved by natural processes. It was suggested that assuming peat is present, a good clean-up approach may be to contain the contaminant source, monitor the lateral and vertical extent of contamination, and wait for natural processes to resolve the problem. 3 figs

  17. Experimental research on quality features of metallurgical coke

    Science.gov (United States)

    Andrei, V.; Constantin, N.

    2015-06-01

    From all the solid fuels, the metallurgical coke is the most used in obtaining iron in the blast furnace. Together with the iron ore, manganese ore and fluxes, it constitutes the basis of raw materials and materials for elaborating pig iron. This paper presents the results of laboratory investigations by the authors to determine the most important quality characteristics of some types of coke used in the blast furnace charge.

  18. Mathematical modeling of a rotary hearth coke calciner

    Directory of Open Access Journals (Sweden)

    Hilde C. Meisingset

    1995-10-01

    Full Text Available A mathematical model of a rotary hearth coke calciner is developed. The model is based on first principles including the most important dynamic phenomena. The model is a thermodynamic model involving heat and mass transfer and chemical reactions. Fundamental mass and energy balance equations for the coke phase, the gas phase and the lining are formulated. For the gas phase, a stationary model is used. The equations are solved numerically, and simulated temperature profiles are shown in this paper.

  19. Coke formation during thermal cracking of a heavy crude oil

    OpenAIRE

    Urán Castaño, Laura Cristina

    2015-01-01

    Abstract: A pseudo-mechanism for the production of coke during the thermal cracking of a Colombian heavy crude oil was proposed based on thermal cracking experiments carried out at TGA and at horizontal tube furnace at atmospheric conditions. In-situ combustion (ISC) is a thermal method that improves the recovery of heavy crude oils and involves complex phenomena such as heat and mass transfers, low-temperature oxidation of the liquid phase (LTO), and cracking reactions that yield coke, a car...

  20. Mathematical modeling of a rotary hearth coke calciner

    OpenAIRE

    Hilde C. Meisingset; Jens G. Balchen

    1995-01-01

    A mathematical model of a rotary hearth coke calciner is developed. The model is based on first principles including the most important dynamic phenomena. The model is a thermodynamic model involving heat and mass transfer and chemical reactions. Fundamental mass and energy balance equations for the coke phase, the gas phase and the lining are formulated. For the gas phase, a stationary model is used. The equations are solved numerically, and simulated temperature profiles are shown in this p...