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Sample records for clean coke process

  1. 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.

  2. 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...

  3. 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 ℃.

  4. 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.

  5. 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

  6. 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.

  7. 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

    2016-06-08

    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.

  8. Research on the evolvement of morphology of coking coal during the coking process.

    Science.gov (United States)

    Zhong, Xiangyun; Wu, Shiyong; Liu, Yang; Zhao, Zhenning; Zhang, Yaru; Bai, Jinfeng; Xu, Jun; Xi, Bai

    2013-12-01

    The evolvement of morphology and structure of the coal with different metamorphic degrees during coking process in the vertical furnace was investigated by infrared Image detector. Moreover, the temperature distribution in the radial direction and the crack formation were also studied in heating process. The results show that the amount of crack and the shrinkage level of char decrease with the coal rank rising. In addition, the initial temperature of crack formation for char increases with the coal rank rising.

  9. 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.

  10. 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.

  11. Integrated coke, asphalt and jet fuel production process and apparatus

    Science.gov (United States)

    Shang, Jer Y.

    1991-01-01

    A process and apparatus for the production of coke, asphalt and jet fuel m a feed of fossil fuels containing volatile carbon compounds therein is disclosed. The process includes the steps of pyrolyzing the feed in an entrained bed pyrolyzing means, separating the volatile pyrolysis products from the solid pyrolysis products removing at least one coke from the solid pyrolysis products, fractionating the volatile pyrolysis products to produce an overhead stream and a bottom stream which is useful as asphalt for road pavement, condensing the overhead stream to produce a condensed liquid fraction and a noncondensable, gaseous fraction, and removing water from the condensed liquid fraction to produce a jet fuel-containing product. The disclosed apparatus is useful for practicing the foregoing process. the process provides a useful method of mass producing and jet fuels from materials such as coal, oil shale and tar sands.

  12. 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.

  13. 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...

  14. 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.

  15. 高硫石油焦清洁利用技术浅析%Simply Analysis of Clean Utilization Technologies in High-Sulfur Petroleum Coke

    Institute of Scientific and Technical Information of China (English)

    徐可忠; 缪超; 宋爱萍

    2011-01-01

    简单介绍了高硫石油焦的性质,概括介绍了高硫石油焦在活性炭生产、铝用预焙阳极生产和立窑水泥生产方面的应用现状,重点论述了循环流化床(CFB)锅炉燃烧技术、POX技术和整体式气化联合循环技术(IGCC)技术的工艺流程、技术特点,以及清洁利用高硫石油焦的发展现状,指出了六种技术在清洁利用高硫石油焦方面的各自不同前景。%The character of high-sulfur petroleum coke was briefly introduced,and the applications of it in activated carbon preparation,production of aluminum prebake anode and cement in shaft kiln were summarized.Three kinds of technologies including circulating fluidized bed(CFB) boiler,partial oxidation(POX) and integrated gasification combined cycle(IGCC) unit were importantly analyzed on process,technical advantage,and the development of clean utilization in high-sulfur petroleum coke.The respective prospect of the six kinds of technologies above in processing high-sulfur petroleum coke were pointed out.

  16. 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.

  17. Visualization of coke state in hydraulic decoking process

    Science.gov (United States)

    Guo, Qian; Tong, Xinglin; Deng, Chengwei; Zhang, Cui; Huang, Di; Chen, Liang; Xiong, Jiaguo

    2016-05-01

    The relationship model of the sound signal and the coke state can be established through multiple test and comparison of the noise signal and the coke operation. By collecting data, we summarize the main frequency power fluctuation range of the sound signal in kinds of state, and extract the nearest 5 decision results for reference. The weighted value of each result according to the update time has gradually increased. On the basis of that, we developed visualization software, real-time reflect out coke coking tower state. Animation refresh rate is second level, and the vertical height can be accurate to 0.1m.

  18. 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.

  19. 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

  20. High pressure water decoking and cleaning for oil and gas lines in delayed coking unit%延迟焦化装置油气管线高压水清焦、清洗

    Institute of Scientific and Technical Information of China (English)

    窦如松; 陈珍

    2012-01-01

    The coke tower to the fractionation tower segment DN500 high pressure oil and gas lines observant coke, used in the cleaning process steps and the correct equipment, nozzle selection to reach a clear focus, cleaning effect, while the construction process safety and environmental protection measures to ensure the health safety and installation of equipment and facilities, non-polluting.%阐述焦炭塔顶至分馏塔段DN500mm油气线高压水清焦、清洗时所采用的工艺步骤及正确的设备、喷头选型使其达到良好的清焦、清洗效果,同时施工过程中所采取的安全环保措施保证人员的健康安全和装置设备设施的无污染。

  1. 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

  2. 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 ...

  3. 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.

  4. 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.

  5. 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...

  6. 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)

  7. 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.

  8. 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...

  9. 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.

  10. ASRM process development in aqueous cleaning

    Science.gov (United States)

    Swisher, Bill

    1992-12-01

    Viewgraphs are included on process development in aqueous cleaning which is taking place at the Aerojet Advanced Solid Rocket Motor (ASRM) Division under a NASA Marshall Space and Flight Center contract for design, development, test, and evaluation of the ASRM including new production facilities. The ASRM will utilize aqueous cleaning in several manufacturing process steps to clean case segments, nozzle metal components, and igniter closures. ASRM manufacturing process development is underway, including agent selection, agent characterization, subscale process optimization, bonding verification, and scale-up validation. Process parameters are currently being tested for optimization utilizing a Taguci Matrix, including agent concentration, cleaning solution temperature, agitation and immersion time, rinse water amount and temperature, and use/non-use of drying air. Based on results of process development testing to date, several observations are offered: aqueous cleaning appears effective for steels and SermeTel-coated metals in ASRM processing; aqueous cleaning agents may stain and/or attack bare aluminum metals to various extents; aqueous cleaning appears unsuitable for thermal sprayed aluminum-coated steel; aqueous cleaning appears to adequately remove a wide range of contaminants from flat metal surfaces, but supplementary assistance may be needed to remove clumps of tenacious contaminants embedded in holes, etc.; and hot rinse water appears to be beneficial to aid in drying of bare steel and retarding oxidation rate.

  11. 清洁型热回收焦炉节能措施%Energy conservation measures of cleaning heat recovery coke oven

    Institute of Scientific and Technical Information of China (English)

    要长维; 薛恺; 李振文; 王慎国

    2011-01-01

    Based on the operation condition of SYR stamping and cleaning heat recovery coke oven, emphasize the main factors affecting energy consumption such as market factors, burn-off rate, water content of coal as fired. According to the (Access Conditions of Coking Industry) (2008 amendment) ,put forward reasonable suggestions to reduce energy consumption and improve benefit of enterprises.%结合SYR型捣固式清洁型热回收焦炉运行状况,着重分析影响其能耗的主要因素,包括市场因素、烧失率、入炉煤水分等,针对这些影响因素并根据《焦化行业准入条件》(2008年修订)相关要求,为进一步降低企业能耗,提高企业效益提出合理化建议.

  12. 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 ...

  13. 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...

  14. 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.

  15. 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%。

  16. 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

  17. 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.

  18. 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.

  19. Effect of coking conditions on Rankin coefficient of coke cake

    Energy Technology Data Exchange (ETDEWEB)

    Arima, T.; Fukuda, K.; Kato, K. [Nippon Steel Corp. Ltd., Futtsu (Japan). Environmental & Process Technology Center

    2004-09-01

    An innovative cokemaking process, SCOPE21 (Super Coke Oven for Productivity and Environmental enhancement toward the 21st century), has been developed by JISF (The Japan Iron and Steel Federation) and CCUJ (Center for Coal Utilization, Japan). As a cokemaking process, it is important to guarantee safe and stable pushing. Coke pushing behavior was studied by using a pilot-scale coke oven and influence of coking conditions on the Rankin coefficient was investigated. It was found that Rankin coefficient was dependent on lateral shrinkage and fissure density in coke cake and that it can be controlled by controlling the fissure density in SCOPE21 process.

  20. 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...

  1. 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.

  2. 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.

  3. 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.

  4. 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.

  5. Quantitative analysis of ammonium salts in coking industrial liquid waste treatment process based on Raman spectroscopy

    Science.gov (United States)

    Cao, Ya-Nan; Wang, Gui-Shi; Tan, Tu; Cai, Ting-Dong; Liu, Kun; Wang, Lei; Zhu, Gong-Dong; Mei, Jiao-Xu

    2016-10-01

    Quantitative analysis of ammonium salts in the process of coking industrial liquid waste treatment is successfully performed based on a compact Raman spectrometer combined with partial least square (PLS) method. Two main components (NH4SCN and (NH4)2S2O3) of the industrial mixture are investigated. During the data preprocessing, wavelet denoising and an internal standard normalization method are employed to improve the predicting ability of PLS models. Moreover, the PLS models with different characteristic bands for each component are studied to choose a best resolution. The internal and external calibration results of the validated model show a mass percentage error below 1% for both components. Finally, the repeatabilities and reproducibilities of Raman and reference titration measurements are also discussed. Project supported by the National Natural Science Foundation of China (Grant Nos. 41405022 and 61475068).

  6. ANALYSIS ON TECHNOLOGICAL PROCESSES CLEANING OIL PIPELINES

    Directory of Open Access Journals (Sweden)

    Mariana PǍTRAŞCU

    2015-05-01

    Full Text Available In this paper the researches are presented concerning the technological processes of oil pipelines.We know several technologies and materials used for cleaning the sludge deposits, iron and manganese oxides, dross, stone, etc.de on the inner walls of drinking water pipes or industries.For the oil industry, methods of removal of waste materials and waste pipes and liquid and gas transport networks are operations known long, tedious and expensive. The main methods and associated problems can be summarized as follows: 1 Blowing with compressed air.2 manual or mechanical brushing, sanding with water or dry.3 Wash with water jet of high pressure, solvent or chemical solution to remove the stone and hard deposits.4 The combined methods of cleaning machines that use water jets, cutters, chains, rotary heads cutters, etc.

  7. Processes forming Gas, Tar, and Coke in Cellulose Gasification from Gas-Phase Reactions of Levoglucosan as Intermediate.

    Science.gov (United States)

    Fukutome, Asuka; Kawamoto, Haruo; Saka, Shiro

    2015-07-01

    The gas-phase pyrolysis of levoglucosan (LG), the major intermediate species during cellulose gasification, was studied experimentally over the temperature range of 400-900 °C. Gaseous LG did not produce any dehydration products, which include coke, furans, and aromatic substances, although these are characteristic products of the pyrolysis of molten LG. Alternatively, at >500 °C, gaseous LG produced only fragmentation products, such as noncondensable gases and condensable C1 -C3 fragments, as intermediates during noncondensable gas formation. Therefore, it was determined that secondary reactions of gaseous LG can result in the clean (tar- and coke-free) gasification of cellulose. Cooling of the remaining LG in the gas phase caused coke formation by the transition of the LG to the molten state. The molecular mechanisms that govern the gas- and molten-phase reactions of LG are discussed in terms of the acid catalyst effect of intermolecular hydrogen bonding to promote the molten-phase dehydration reactions. PMID:26099988

  8. Processes forming Gas, Tar, and Coke in Cellulose Gasification from Gas-Phase Reactions of Levoglucosan as Intermediate.

    Science.gov (United States)

    Fukutome, Asuka; Kawamoto, Haruo; Saka, Shiro

    2015-07-01

    The gas-phase pyrolysis of levoglucosan (LG), the major intermediate species during cellulose gasification, was studied experimentally over the temperature range of 400-900 °C. Gaseous LG did not produce any dehydration products, which include coke, furans, and aromatic substances, although these are characteristic products of the pyrolysis of molten LG. Alternatively, at >500 °C, gaseous LG produced only fragmentation products, such as noncondensable gases and condensable C1 -C3 fragments, as intermediates during noncondensable gas formation. Therefore, it was determined that secondary reactions of gaseous LG can result in the clean (tar- and coke-free) gasification of cellulose. Cooling of the remaining LG in the gas phase caused coke formation by the transition of the LG to the molten state. The molecular mechanisms that govern the gas- and molten-phase reactions of LG are discussed in terms of the acid catalyst effect of intermolecular hydrogen bonding to promote the molten-phase dehydration reactions.

  9. Physical cleaning of high carbon fly ash

    Energy Technology Data Exchange (ETDEWEB)

    Gray, McMahan L.; Champagne, Kenneth J.; Soong, Yee; Killmeyer, Richard P. [National Energy Technology Laboratory, US Department of Energy, P.O. Box 10940, Cochran Mills Roads, 15236 Pittsburgh, PA (United States); Maroto-Valer, M. Mercedes; Andresen, John M. [The Energy Institute, The Pennsylvania State University, 405 Academic Activities Building, 16802-2308 University Park, PA (United States); Ciocco, Michael V.; Zandhuis, Paul H. [Parson Project Services Inc, National Energy Technology Laboratory, P.O. Box 618, 15129 Library, Pittsburgh, PA (United States)

    2002-04-20

    An industrial fly ash sample was cleaned by three different processes, which were triboelectrostatic separation, ultrasonic column agglomeration, and column flotation. The unburned carbon concentrates were collected at purities ranging up to 62% at recoveries of 62%. In addition, optical microscopy studies were conducted on the final carbon concentrates to determine the carbon forms (inertinite, isotropic coke and anisotropic coke) collected from these various physical-cleaning processes. The effects of the various cleaning processes on the production of different carbon forms from high carbon fly ashes will be discussed.

  10. 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

  11. 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.

  12. 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

  13. 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...

  14. 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.

  15. 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

  16. 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

  17. 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.

  18. 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.

  19. 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

  20. 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.

  1. 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.

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

    Institute of Scientific and Technical Information of China (English)

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

    2013-01-01

    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.

  3. 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...

  4. 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.

  5. 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。

  6. 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...

  7. 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

  8. 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.

  9. 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.

  10. 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 ...

  11. 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...

  12. ENHANCED CHEMICAL CLEANING: A NEW PROCESS FOR CHEMICALLY CLEANING SAVANNAH RIVER WASTE TANKS

    Energy Technology Data Exchange (ETDEWEB)

    Ketusky, E; Neil Davis, N; Renee Spires, R

    2008-01-17

    The Savannah River Site (SRS) has 49 high level waste (HLW) tanks that must be emptied, cleaned, and closed as required by the Federal Facilities Agreement. The current method of chemical cleaning uses several hundred thousand gallons per tank of 8 weight percent (wt%) oxalic acid to partially dissolve and suspend residual waste and corrosion products such that the waste can be pumped out of the tank. This adds a significant quantity of sodium oxalate to the tanks and, if multiple tanks are cleaned, renders the waste incompatible with the downstream processing. Tank space is also insufficient to store this stream given the large number of tanks to be cleaned. Therefore, a search for a new cleaning process was initiated utilizing the TRIZ literature search approach, and Chemical Oxidation Reduction Decontamination--Ultraviolet (CORD-UV), a mature technology currently used for decontamination and cleaning of commercial nuclear reactor primary cooling water loops, was identified. CORD-UV utilizes oxalic acid for sludge dissolution, but then decomposes the oxalic acid to carbon dioxide and water by UV treatment outside the system being treated. This allows reprecipitation and subsequent deposition of the sludge into a selected container without adding significant volume to that container, and without adding any new chemicals that would impact downstream treatment processes. Bench top and demonstration loop measurements on SRS tank sludge stimulant demonstrated the feasibility of applying CORD-UV for enhanced chemical cleaning of SRS HLW tanks.

  13. South Africa faces coke shortage

    Energy Technology Data Exchange (ETDEWEB)

    NONE

    1998-05-01

    Iscor Vanderbijlpark in South Africa may need to import substantial tonnages of coking coal as a result of increasing quality demands on coke at Vanderbiljpark (to support the recently installed PCI process) as well as the Newcastle works. Availability of coke is not only a problem for the South African steel industry but is a global problem as the production of coke in Western countries has declined over the past three years. A massive expansion in coke-making capacity is happening in China but the Chinese beehive ovens create serious pollution problems. A world shortage of coke of 30 million t/y by 2005 is estimated, rising to over 60 million t/y by 2010 of no new capacity is created. Steelmakers have succeeded in reducing their consumption of coke, by pulverised coal injection by better distribution of components in the furnace shaft and by decline in use of the blast furnace-basic oxygen furnace route, but the industry is still facing serious shortages of coke.

  14. Prioritizing substitution of organic solvents in industrial cleaning processes

    DEFF Research Database (Denmark)

    Rasmussen, Pia Brunn; Jacobsen, Thomas

    1997-01-01

    A method for prioritizing the substitution of volatile organic compounds (VOC) used in industrial cleaning processes is developed. The result is a matrix, which, if all information can be obtained, gives a comprehensive description of the effects, exposure and emission of VOC, as well...... as the prospects for performing the substitution with a vegetable ester. It can be a tool for companies to decide which cleaning process has the highest demand for substitution, if there is a choice between several processes, but it may also be a tool to convince companies to use non-volatile, low-toxic cleaning...

  15. 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.

  16. 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...

  17. 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。

  18. 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...

  19. 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.

  20. 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 ...

  1. Continuous coking of heavy feedstocks

    Energy Technology Data Exchange (ETDEWEB)

    Sullivan, Douglas W. [Lidcon, Inc (United States)

    2011-07-01

    A new process for continuous coking and decoking has been developed by Lidcon Inc. This process uses bitumen, vacuum tower residues, or a heavy CCR stock. The Lidcon process produces a higher liquid yield and lowers solid coke production. It also reduces the effects on the environment by lowering the amount of utilities that are needed to power the unit, while improving fire and worker safety. The reactor also produces coke continuously. The theoretical advantage of such a reactor configuration is that it has a short high temperature residence time for volatiles while improving the mass transfer of volatiles through the residue. The dimensions of the reactor are approximately 28' long with a 7' diameter. The weight of the unit is 20,000lbs. The Lidcon process can deliver a higher level of efficiency while reducing the amount of coke that is produced.

  2. 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.

  3. 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...

  4. 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...

  5. 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。

  6. 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.

  7. 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.

  8. 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...

  9. 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

  10. 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......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......, 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....

  11. Enhanced Chemical Cleaning: A New Process for Chemically Cleaning Savannah River Waste Tanks

    Energy Technology Data Exchange (ETDEWEB)

    Ketusky, Edward; Spires, Renee; Davis, Neil

    2009-02-11

    At the Savannah River Site (SRS) there are 49 High Level Waste (HLW) tanks that eventually must be emptied, cleaned, and closed. The current method of chemically cleaning SRS HLW tanks, commonly referred to as Bulk Oxalic Acid Cleaning (BOAC), requires about a half million liters (130,000 gallons) of 8 weight percent (wt%) oxalic acid to clean a single tank. During the cleaning, the oxalic acid acts as the solvent to digest sludge solids and insoluble salt solids, such that they can be suspended and pumped out of the tank. Because of the volume and concentration of acid used, a significant quantity of oxalate is added to the HLW process. This added oxalate significantly impacts downstream processing. In addition to the oxalate, the volume of liquid added competes for the limited available tank space. A search, therefore, was initiated for a new cleaning process. Using TRIZ (Teoriya Resheniya Izobretatelskikh Zadatch or roughly translated as the Theory of Inventive Problem Solving), Chemical Oxidation Reduction Decontamination with Ultraviolet Light (CORD-UV{reg_sign}), a mature technology used in the commercial nuclear power industry was identified as an alternate technology. Similar to BOAC, CORD-UV{reg_sign} also uses oxalic acid as the solvent to dissolve the metal (hydr)oxide solids. CORD-UV{reg_sign} is different, however, since it uses photo-oxidation (via peroxide/UV or ozone/UV to form hydroxyl radicals) to decompose the spent oxalate into carbon dioxide and water. Since the oxalate is decomposed and off-gassed, CORD-UV{reg_sign} would not have the negative downstream oxalate process impacts of BOAC. With the oxalate destruction occurring physically outside the HLW tank, re-precipitation and transfer of the solids, as well as regeneration of the cleaning solution can be performed without adding additional solids, or a significant volume of liquid to the process. With a draft of the pre-conceptual Enhanced Chemical Cleaning (ECC) flowsheet, taking full

  12. 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.

  13. 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

  14. 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)

  15. 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

  16. 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.

  17. 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

  18. 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...

  19. 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)

  20. Alternatives to Organic Solvents in Industrial Cleaning Processes

    DEFF Research Database (Denmark)

    Jacobsen, Thomas

    1998-01-01

    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...... 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...

  1. 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

  2. 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

  3. 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.

  4. 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)

  5. 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

  6. 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

  7. Membrane Bioreactor (MBR) Processes for Treatment of Coking Wastewater%焦化废水的MBR处理工艺

    Institute of Scientific and Technical Information of China (English)

    刘国正; 何义亮

    2013-01-01

    针对焦化废水治理难题,将传统生化处理工艺A/A/O改造成A/A/O+MBR组合处理工艺,运行结果表明:A/A/O+MBR组合工艺对NH3-N去除效果好,处理出水NH3-N浓度一般为5~10 mg/L,CODcr浓度为200 mg/L左右,较A/A/O工艺有明显改善和提高;剩余污泥产量为系统改造前的10%左右,大大节约了污泥处理处置成本;MBR膜组件模块化自动控制,简化了操作维护,有效减缓了膜污染.%Advanced treatment for coking wastewater was investigated experimentally by A/A/O+MBR combination treatment process, due to the water quality usually could not meet the discharge standards after conventional biological treatment A/A/O process. The results showed that A/A/O+MBR was more effective than A/A/O process for removing ammonia nitrogen (NH3-N) and other refractory compounds. The concentration of NH3-N and CODGr after the treatment by A/A/O+MBR process were 5~10 mg/L and 200 mg/L, respectively. Moreover, it was found that the excessive sludge yielded reduced by 10 % relatived to the system before the transformation, which was a significant reduction in the cost of sludge treatment and disposal. Also, modular-automatic control of MBR membrane modules simplified the operation and maintenance, and eliminated the membrane fouling effectively.

  8. 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.

  9. 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...

  10. 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。

  11. 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.

  12. 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...

  13. Study on occurrence of sulfur in different group components of Xinyu clean coking coal%新峪焦精煤中硫在族组分间的赋存规律研究

    Institute of Scientific and Technical Information of China (English)

    秦志宏; 张豪非; 戴冬瑾; 赵翠翠; 张丽芳

    2014-01-01

    This paper illustrates the occurrence and distribution of sulfur in coal from the perspective of composition and structure of the coal body.With the organic sulfur-rich Xinyu clean coking coal as the sample, and the method of separating all group components from coal through extraction and stripping process as well as X-ray photoelectron spectroscopy ( XPS ) and gas chromatogrpa hy/masss pectrometer ( GC/MS) analysis techniques, the content of inorganic sulfur and organic slu fur of diffre ent forms in raw cola and various group components isstudied andt he occurrence of organic sulfur in organic matter of coal is carefully observed.The results show the distribution of inorganic sulfur is mainly dependent upon its particle siez and density in coal and has less relationship wti h the structure of group components of coal.Thiophene sulfur ist he major form fo o rganic sufl ur either in raw cola or group components.The ext ernal envri onment of molecules dominated by conjugated structure can derc ease the elector n binding energy of ogr anic sulfur in conjugated structru e, whiel incrae se that of us lfur in aliphatic structure.Th e distribution of organic sulfuri n coal si balanc ed as a whole and will not be signifiac ntly infleu nced by ts rucut ral differne ces of group components. Howve er, the occurrence of organic sulfur compounds is assocai ted with the structure of group components, showing relatively small difference.And there is only one type of small molce ule orag nic sulfur compounds in light component, with small abundance.%为从煤的本体组成结构方面来阐述煤中硫的赋存与分布规律,以高含有机硫的新峪焦精煤为对象,采用萃取反萃取的煤全组分分离方法和XPS、GC/MS等分析技术,对原煤和各族组分中的不同形态无机硫和有机硫含量进行了研究,重点考察了有机硫在煤有机质本体中的赋存规律。结果表明,无机硫的分布主要依赖于其自身在煤主体中

  14. 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)

  15. 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.

  16. Influence of cleaning process on the laser-induced damage threshold of substrates.

    Science.gov (United States)

    Shen, Zhengxiang; Ding, Tao; Ye, Xiaowen; Wang, Xiaodong; Ma, Bin; Cheng, Xinbin; Liu, Huasong; Ji, Yiqin; Wang, Zhanshan

    2011-03-20

    The cleaning process of optical substrates plays an important role during the manufacture of high-power laser coatings. Two kinds of substrates, fused silica and BK7 glass, and two cleaning processes, called process 1 and process 2 having different surfactant solutions and different ultrasonic cleaning parameters, are adopted to compare the influence of the ultrasonic cleaning technique on the substrates. The evaluation standards of the cleaning results include contaminant-removal efficiency, weak absorption, and laser-induced damage threshold of the substrates. For both fused silica and BK7, process 2 is more efficient than process 1. Because acid and alkaline solutions can increase the roughness of BK7, process 2 is unsuitable for BK7 glass cleaning. The parameters of the cleaning protocol should be changed depending on the material of the optical components and the type of contamination.

  17. 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.

  18. 电絮凝用于焦化废水脱色的研究%Study on decolorization of coking wastewater by continuous electrocoagulation process

    Institute of Scientific and Technical Information of China (English)

    张垒; 薛改凤; 张楠; 刘尚超; 段爱民; 刘璞

    2011-01-01

    The decolorization and chemical oxygen demand(COD) reduction of coking wastewater has been carried out by electrocoagulation process.In the meanwhile effects of operating parameters,such as current density,pH of solution,electrolyte concentration and hydraulic residence time(HRT) on decolorization by continuous electrocoagulation are further studied in order to optimize process performance.The UV-Vis spectrum data proves that organic pollutants of the coking wastewater can be effectively degraded and decolorized by electrocoagulation.Results show that the effects of electrocoagulation process on the decolorization of the coking wastewater are obvious and up to 91% of color removal efficiency is obtained after 80 min reaction at 25 ℃ with a current density of 30 mA /cm2,a pH of 8.0,an electrode distance of 1.0 cm and a supporting electrolyte concentration of 0.5 g /L.%采用了连续电絮凝工艺对焦化废水进行深度处理,考察了电流密度、溶液pH值、电解质密度和水力停留时间等工艺参数对脱色效率的影响。UV-Vis谱图证实了电絮凝能有效地对有机物进行降解和脱色。结果表明,电絮凝工艺对焦化废水脱色效果明显,当电流密度为30 mA/cm2,pH值为8.0,极板距为1.0 cm,支持电解质浓度为0.5 g/L,在25℃下反应80 min后脱色效率达91%以上。

  19. 可乐鸡翅生产工艺研究%Processing technology of chicken wing with coke

    Institute of Scientific and Technical Information of China (English)

    徐晓霞; 张怀珠; 冯晓群; 彭涛

    2011-01-01

    Chicken wings were taken as raw materials in this paper;single-factor and the orthogonal experiments were employed to study the effects of pickling time,coke content in soup and boiling time on epidermis chromatic difference of chicken wing and sensory quality.The result indicated that pickling for 18h,coke content of 66%,boiling for 25 min,the product was delicious,with brightly color and retained coke flavor.There will be a broad market prospect for this product.%以鸡翅为主要原料,通过单因素试验和正交试验,重点研究腌制时间、煮汤中可乐的百分含量、煮制时间等因素对可乐鸡翅表皮色差和感官品质的影响。结果表明:腌制时间18h,煮汤中可乐的百分含量66%,煮制时间25min。该产品味道鲜美,色泽艳丽,保留了可乐的香气,市场前景广阔。

  20. REDUCING POWER PRODUCTION COSTS BY UTILIZING PETROLEUM COKE

    Energy Technology Data Exchange (ETDEWEB)

    Kevin C. Galbreath; Donald L. Toman; Christopher J. Zygarlicke

    1999-09-01

    Petroleum coke, a byproduct of the petroleum-refining process, is an attractive primary or supplemental fuel for power production primarily because of a progressive and predictable increase in the production volumes of petroleum coke (1, 2). Petroleum coke is most commonly blended with coal in proportions suitable to meet sulfur emission compliance. Petroleum coke is generally less reactive than coal; therefore, the cofiring of petroleum coke with coal typically improves ignition, flame stability, and carbon loss relative to the combustion of petroleum coke alone. Although petroleum coke is a desirable fuel for producing relatively inexpensive electrical power, concerns about the effects of petroleum coke blending on combustion and pollution control processes exist in the coal-fired utility industry (3). The Energy & Environmental Research Center (EERC) completed a 2-year technical assessment of petroleum coke as a supplemental fuel. A survey questionnaire was sent to seven electric utility companies that are currently cofiring coal and petroleum coke in an effort to solicit specific suggestions on research needs and fuel selections. An example of the letter and survey questionnaire is presented in Appendix A. Interest was expressed by most utilities in evaluating the effects of petroleum coke blending on grindability, combustion reactivity, fouling, slagging, and fly ash emissions control. Unexpectedly, concern over corrosion was not expressed by the utilities contacted. Although all seven utilities responded to the question, only two utilities, Northern States Power Company (NSP) and Ameren, sent fuels to the EERC for evaluation. Both utilities sent subbituminous coals from the Power River Basin and petroleum shot coke samples. Petroleum shot coke is produced unintentionally during operational upsets in the petroleum refining process. This report evaluates the effects of petroleum shot coke blending on grindability, fuel reactivity, fouling/slagging, and

  1. 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.

  2. 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.

  3. 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)

  4. 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.

  5. 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.

  6. Tunable droplet momentum and cavitation process for damage-free cleaning of challenging particles

    Science.gov (United States)

    Gouk, Roman; Papanu, James; Li, Fred; Jeon, Jason; Liu, Tong; Yalamanchili, Rao

    2008-10-01

    Particle removal without damage has been demonstrated for cleaning technology that employs NanoDropletTM mixed-fluid jet nozzle. Although 99%+ particle removal efficiency can be achieved for standard Si3N4 particles with broad size distribution, there are some cleaning challenges with small (500nm) particles. It was found that tunable uniform cavitation can provide the additional physical assist force needed to improve cleaning efficiency of these challenging particles while meeting the damage-fee cleaning requirement. An integrated cleaning process was developed that combines both droplet momentum and damage-free cavitation technology. Cleaning tests were performed with different types of challenging particles. The results showed 5-8% particle removal efficiency improvement as compared to momentum based only cleaning. All masks were processed using the TetraTM mask cleaning tool configured with NanoDropletTM mixed fluid jet technology and full face megasonics.

  7. 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...

  8. 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.

  9. 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.

  10. 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.

  11. 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.

  12. 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.

  13. 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.

  14. 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...

  15. Reformation of Ceramic Filter Used in Coke Oven Gas Purification Process%焦炉煤气净化洗涤陶瓷过滤器的改造

    Institute of Scientific and Technical Information of China (English)

    王卫忠

    2012-01-01

    In coke oven gas purification process, tar ammonia liquor separating system treats the residual ammonia wa- ter,ceramic filter filters rich solution. Because the most of tar were not removed by the filter, so the subsequent process and the treatment effect of wastwater were influenced. To ease the influence from tar of system by reforming ceramic filter.%在焦炉煤气净化工艺中,焦油氨水分离系统处理剩余氨水,陶瓷过滤器过滤富液。过滤器未除去大部分焦油,从而影响后续工序正常进行及废水处理效果。通过对陶瓷过滤器进行改造,减轻了系统中焦油带来的影响。

  16. 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.

  17. Study on combustion characteristics of petroleum coke residual oil slurry

    Energy Technology Data Exchange (ETDEWEB)

    Shou Weiyi; Xu Xiaoming; Cao Xinyu [and others

    1997-07-01

    Petroleum coke residual oil slurry (POS) is one of prospect substitute of oil burned in many industrial boilers and utilities in China. It is a mixture of pulverized petroleum coke, residual oil and slurry oil. We carried out a series of experiments to study its ignition and combustion mechanism. Experimental results show that the ignition temperature of petroleum coke is higher than normal anthracite and meager coal, and it is difficult to be burned in oil-fired furnace directly. The petroleum coke`s combustion property is improved greatly after mixing with residual oil and slurry oil. The combustion process of POS can be divided into three phases: preheating, kindling and homogenous combustion, burning of the petroleum coke residue. The combustion condition of POS is close to bituminous and coal-oil-mixture (COM).

  18. 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

  19. 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.

  20. 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.

  1. 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

  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. 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...

  5. 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.

  6. 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.

  7. 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.

  8. 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

  9. 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...

  10. Coke fouling monitoring by electrical resistivity

    Energy Technology Data Exchange (ETDEWEB)

    Bombardelli, Clovis; Mari, Livia Assis; Kalinowski, Hypolito Jose [Universidade Tecnologica Federal do Parana (UTFPR), Curitiba, PR (Brazil). Programa de Pos-Graduacao em Engenharia Eletrica e Informatica Industrial (CPGEI)

    2008-07-01

    An experimental method to simulate the growth of the coke fouling that occurs in the oil processing is proposed relating the thickness of the encrusted coke to its electrical resistivity. The authors suggest the use of the fouling electrical resistivity as a transducer element for determining its thickness. The sensor is basically two electrodes in an electrically isolated device where the inlay can happen in order to compose a purely resistive transducer. Such devices can be easily constructed in a simple and robust form with features capable to face the high temperatures and pressures found in relevant industrial processes. For validation, however, it is needed a relationship between the electrical resistivity and the fouling thickness, information not yet found in the literature. The present work experimentally simulates the growth of a layer of coke on an electrically insulating surface, equipped with electrodes at two extremities to measure the electrical resistivity during thermal cracking essays. The method is realized with a series of consecutive runs. The results correlate the mass of coke deposited and its electrical resistivity, and it can be used to validate the coke depositions monitoring employing the resistivity as a control parameter. (author)

  11. 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...

  12. Coke quality requirements in POSCO

    Energy Technology Data Exchange (ETDEWEB)

    Song, J.; Yi, J.; Wang, H. [POSCO (Republic of Korea). Cokemaking Dept.

    2001-07-01

    The 26 overheads describes coke quality requirements in POSCO, Republic of Korea. It is concluded that it is necessary to develop new coal and to prompt technical development in order to produce high quality coke. To improve coke quality. Posco had applied DMAIC (define, measurement, analysis, improvement, control) technique which is part of Six-Sigma activity.

  13. 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

  14. Experimental and theoretical analysis of the laser shock cleaning process for nanoscale particle removal

    Science.gov (United States)

    Kim, Dongsik; Oh, Bukuk; Jang, Deoksuk; Lee, Jeong-Wook; Lee, Jong-Myoung

    2007-07-01

    The laser shock cleaning (LSC) process has been shown to be effective for removing submicron-sized contaminant particles from solid surfaces and thus bears strong potential in various applications. In this work, experimental and theoretical analysis are conducted to reveal the underlying physical mechanisms of the LSC process, with emphasis on the laser-induced hydrodynamics and the effect of external gas-jet injection through a nozzle. A two-dimensional theoretical model is proposed for rigorous simulation of the hydrodynamic phenomena occurring in the LSC process. The hydrodynamics computed by the model is in qualitative agreement with experimental observations and reveal the details of the physics involved in the cleaning process. The effect of gas blowing on the cleaning performance is analyzed both experimentally and theoretically. The results indicate that the gas flow can significantly change the hydrodynamics and increase the cleaning efficiency by reducing the chance of particle redeposition.

  15. Optimization of operating condition for process of catalytic oxidative adsorption desulfurization of coking diesel%焦化柴油催化氧化吸附脱硫工艺条件优化

    Institute of Scientific and Technical Information of China (English)

    张华军; 闫锋; 廖克俭; 兰艳

    2011-01-01

    以磷钼酸季铵盐为催化剂,三氟乙酸为氧化剂,糠醛为萃取剂,采用催化氧化-萃取吸附组合工艺对焦化柴油进行脱硫处理.结果表明,在反应温度为60℃,氧化剂用量(V(氧化剂)/V(焦化柴油))为0.2,催化剂用量(m(催化剂)/V(焦化柴油))为8 g/L,反应时间为60 min,萃取剂用量(V(萃取剂)/V(焦化柴油))为1.0,萃取时间为30 min的最佳工艺条件下,焦化柴油的硫质量分数可从1.05×10-3下降为42×10-6.%The deep desulfurization of coking diesel was investigated by catalytic oxidation -extraction- adsorption combination process with quaternary ammonium phosphomolybdate as catalyst,trifluoroacetic acid as oxidant, furfural as extractant.The results showed that under the optimal condition of reaction temperature of 60 ℃, volume ratio of oxidant to coking diesel of 0.2, catalyst mass concentration in coking diesel of 8 g/L, reaction time of 60 min,volume ratio of extractant to coking diesel of 1.0 and extraction time of 30 min, the mass fraction of sulfur in coking diesel could decrease from 1.05 × 10-3 to 42 × 10-6

  16. 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

  17. 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

  18. 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

  19. 用生物脱氮工艺处理焦化废水%Treatment of coking waste by bio-denitrifying process

    Institute of Scientific and Technical Information of China (English)

    郭建辉

    2001-01-01

    A process of wastewater treatment is introduced. Cultivation, docility, operation management and problems existing in sewage treatment are stressed. The process contains three steps as follows,pre-treatment,bio-treatment and post-treatment including an anaerobic sewage treatment process. The rate of de nitrifying and deammoniation is more than 60% ,and the rate of reduction of COD is more than 70%.The water after treatment can be used for extinction of coke and coal washing.%介绍了采用A2/O生物脱氮工艺处理焦化废水的工艺流程,重点用述了污泥的培养、驯化和运行管理及应注意的问题。该工艺特点在于在一般缺氧-好氧工艺的基础上增加厌氧工段,从而较好地对污水水解酸化,提高处理效率。氨氯去除率大于60%,COD去除率大于70%,处理后的回用水水质符合工艺要求,用作熄焦及洗煤补充水。

  20. High coking value pitch

    Energy Technology Data Exchange (ETDEWEB)

    Miller, Douglas J.; Chang, Ching-Feng; Lewis, Irwin C.; Lewis, Richard T.

    2014-06-10

    A high coking value pitch prepared from coal tar distillate and has a low softening point and a high carbon value while containing substantially no quinoline insolubles is disclosed. The pitch can be used as an impregnant or binder for producing carbon and graphite articles.

  1. Separation of mercury in industrial processes of Polish hard steam coals cleaning

    Directory of Open Access Journals (Sweden)

    Wierzchowski Krzysztof

    2016-01-01

    Full Text Available Coal use is regarded as one of main sources of anthropogenic propagation of mercury in the environment. The coal cleaning is listed among methods of the mercury emission reduction. The article concerns the statistical assessment of mercury separation between coal cleaning products. Two industrial processes employed in the Polish coal preparation plants are analysed: coal cleaning in heavy media vessels and coal cleaning in jigs. It was found that the arithmetic mean mercury content in coarse and medium coal size fractions for clean coal from heavy media vessels, amounts 68.9 μg/kg, and most of the results lay below the mean value, while for rejects it amounts 95.5 μg/kg. It means that it is for around 25 μg/kg greater than in the clean coal. The arithmetic mean mercury content in raw coal smalls amounts around 118 mg/kg. The cleaning of smalls in jigs results in clean coal and steam coal blends characterized by mean mercury content 96.8 μg/kg and rejects with mean mercury content 184.5 μg/kg.

  2. 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.

  3. 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.

  4. 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.

  5. 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.

  6. 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.

  7. Organic pollution removal from coke plant wastewater using coking coal.

    Science.gov (United States)

    Gao, Lihui; Li, Shulei; Wang, Yongtian; Sun, Hao

    2015-01-01

    Coke plant wastewater (CPW) is an intractable chemical wastewater, and it contains many toxic pollutants. This article presents the results of research on a semi-industrial adsorption method of coking wastewater treatment. As a sorbent, the coking coal (CC) was a dozen times less expensive than active carbon. The treatment was conducted within two scenarios, as follows: (1) adsorption after biological treatment of CPW with CC at 40 g L(-1); the chemical oxygen demand (COD) removal was 75.66%, and the concentration was reduced from 178.99 to 43.56 mg L(-1); (2) given an adsorption by CC of 250 g L(-1) prior to the biological treatment of CPW, the eliminations of COD and phenol were 58.08% and 67.12%, respectively. The CC that adsorbed organic pollution and was returned to the coking system might have no effect on both coke oven gas and coke. PMID:26114284

  8. 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

  9. ECR plasma cleaning: an in-situ processing technique for RF cavities

    Energy Technology Data Exchange (ETDEWEB)

    Wu, G.; /Fermilab; Moeller, W-D.; /DESY; Antoine, C.; /Saclay; Jiang, H.; Pechenezhskiy, I.; Cooley, L.; Khabiboulline, T.; Terechkine, Y.; Edwards, H.; Koeth, T.; Romanenko, A.; /Cornell U., Phys. Dept. /Jefferson Lab

    2008-01-01

    A condition for Electron Cyclotron Resonance (ECR) can be established inside a fully assembled RF cavity without the need for removing high-power couplers. As such, plasma generated by this process can be used as a final cleaning step, or as an alternative cleaning step in place of other techniques. Tests showed filtered dry air plasma can successfully remove sulfur particles on niobium surface while the surface oxygen content remains intact.

  10. 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.

  11. 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.

  12. 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.

  13. 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

  14. 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.

  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. Alternative method for assessing coking coal plasticity

    Energy Technology Data Exchange (ETDEWEB)

    Dzuy Nguyen; Susan Woodhouse; Merrick Mahoney [University of Adelaide (Australia). BHP Billiton Newcastle Technology Centre

    2008-07-15

    Traditional plasticity measurements for coal have a number of limitations associated with the reproducibility of the tests and their use in predicting coking behaviour. This report reviews alternative rheological methods for characterising the plastic behaviour of coking coals. It reviews the application of more fundamental rheological measurements to the coal system as well as reviewing applications of rheology to other physical systems. These systems may act as potential models for the application of fundamental rheological measurements to cokemaking. The systems considered were polymer melts, coal ash melts, lava, bread making and ice cream. These systems were chosen because they exhibit some physically equivalent processes to the processes occurring during cokemaking, eg, the generation of bubbles within a softened system that then resolidifies. A number of recommendations were made; the steady and oscillatory shear squeeze flow techniques be further investigated to determine if the measured rheology characteristics are related to transformations within the coke oven and the characteristics of resultant coke; modification of Gieseler plastometers for more fundamental rheology measurements not be attempted.

  17. A novel wastewater cleaning system for the stone-crushing and sand-making process

    Institute of Scientific and Technical Information of China (English)

    Zhang Wenjun; Li Yanfeng; Tang Jie

    2012-01-01

    The nature of the slurry from the stone-crushing and sand-making processes is analyzed to develop a novel separation process.The process comprises hydro-cyclone separation followed by screening of the fines,clarification,and filtration.Recovering fine sand and clean wastewater for recycle is demonstrated.The +0.045 mm fine sand fraction and-0.045 mm ultra-fine clay in the slurry are separated and recovered.Fine sand that was previously lost and wasted is now recoverable.The cleaned and reused water is as much as 94% of the total.

  18. 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.

  19. 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.

  20. 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.).

  1. 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.)

  2. 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

  3. 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 ...

  4. 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

  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. 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.

  9. 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...

  10. 2000 Annual report NATO/CCMS Pilot Study, Clean Products and Processes (Phase I)

    DEFF Research Database (Denmark)

    Wenzel, Henrik; Molin, Christine; Hauschild, Michael Zwicky;

    2001-01-01

    The NATO/Committee on the Challenges of Modern Society third Pilot Study meeting on Clean Products and Processes was held in Copenhagen, Denmark on May 7-12, 2000. This meeting maintained the momentum generated during the of the first two years of the pilot study, focusing on progress made...

  11. 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...

  12. 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.

  13. 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.

  14. 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.

  15. 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.

  16. 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...

  17. 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.

  18. 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.

  19. Use of Synthetic Single-Stranded Oligonucleotides as Artificial Test Soiling for Validation of Surgical Instrument Cleaning Processes

    Directory of Open Access Journals (Sweden)

    Nadja Wilhelm

    2014-01-01

    Full Text Available Surgical instruments are often strongly contaminated with patients’ blood and tissues, possibly containing pathogens. The reuse of contaminated instruments without adequate cleaning and sterilization can cause postoperative inflammation and the transmission of infectious diseases from one patient to another. Thus, based on the stringent sterility requirements, the development of highly efficient, validated cleaning processes is necessary. Here, we use for the first time synthetic single-stranded DNA (ssDNA_ODN, which does not appear in nature, as a test soiling to evaluate the cleaning efficiency of routine washing processes. Stainless steel test objects were coated with a certain amount of ssDNA_ODN. After cleaning, the amount of residual ssDNA_ODN on the test objects was determined using quantitative real-time PCR. The established method is highly specific and sensitive, with a detection limit of 20 fg, and enables the determination of the cleaning efficiency of medical cleaning processes under different conditions to obtain optimal settings for the effective cleaning and sterilization of instruments. The use of this highly sensitive method for the validation of cleaning processes can prevent, to a significant extent, the insufficient cleaning of surgical instruments and thus the transmission of pathogens to patients.

  20. 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.

  1. 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%。

  2. 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.

  3. 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.

  4. Temporal pulse cleaning by a self-diffraction process for ultrashort laser pulses

    Science.gov (United States)

    Xie, Na; Zhou, Kainan; Sun, Li; Wang, Xiaodong; Guo, Yi; Li, Qing; Su, Jingqin

    2014-11-01

    Applying the self-diffraction process to clean ultrashort laser pulses temporally is a recently developed effective way to temporal contrast enhancement. In this paper, we attempt to clean ultrashort laser pulses temporally by the self-diffraction process. Experiments were carried out to study the temporal contrast improvement in the front-end system of an ultraintense and ultrashort laser facility, i.e. the super intense laser for experiment on the extremes (SILEX-I). The results show that the maximum conversion efficiency of the first-order self-diffraction (SD1) pulse is 11%. The temporal contrast of the SD1 signal is improved by two orders of magnitude, i.e. to 103, for a 2.4-ns prepulse with initial contrast of ~10. For a 5.5 -ns prepulse with initial contrast of 2×103, the temporal contrast of the SD1 signal is improved by more than three orders of magnitude.

  5. 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.

  6. 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

  7. Effectiveness of bone cleaning process using chemical and entomology approaches: time and cost.

    Science.gov (United States)

    Lai, Poh Soon; Khoo, Lay See; Mohd Hilmi, Saidin; Ahmad Hafizam, Hasmi; Mohd Shah, Mahmood; Nurliza, Abdullah; Nazni, Wasi Ahmad

    2015-08-01

    Skeletal examination is an important aspect of forensic pathology practice, requiring effective bone cleaning with minimal artefact. This study was conducted to compare between chemical and entomology methods of bone cleaning. Ten subjects between 20 and 40 years old who underwent uncomplicated medico-legal autopsies at the Institute of Forensic Medicine Malaysia were randomly chosen for this descriptive cross sectional study. The sternum bone was divided into 4 parts, each part subjected to a different cleaning method, being two chemical approaches i.e. laundry detergent and a combination of 6% hydrogen peroxide and powder sodium bicarbonate and two entomology approaches using 2nd instar maggots of Chrysomyia rufifacies and Ophyra spinigera. A scoring system for grading the outcome of cleaning was used. The effectiveness of the methods was evaluated based on average weight reduction per day and median number of days to achieve the average score of less than 1.5 within 12 days of the bone cleaning process. Using maggots was the most time-effective and costeffective method, achieving an average weight reduction of 1.4 gm per day, a median of 11.3 days to achieve the desired score and an average cost of MYR 4.10 per case to reach the desired score within 12 days. This conclusion was supported by blind validation by forensic specialists achieving a 77.8% preference for maggots. Emission scanning electron microscopy evaluation also revealed that maggots especially Chrysomyia rufifacies preserved the original condition of the bones better allowing improved elucidation of bone injuries in future real cases.

  8. Experimental study on delayed coking process with coal tar pitch%煤焦油沥青延迟焦化工艺试验研究

    Institute of Scientific and Technical Information of China (English)

    王洪彬; 黄新龙; 李节; 刘淑芳

    2012-01-01

    在选定的条件下,对煤焦油沥青进行了延迟焦化工艺试验,结果表明:以煤沥青直接作为焦化进料时,可以获得质量分数为10% ~ 20%的液体产品;以煤沥青混兑蒽油为延迟焦化进料时,其液体收率大幅提高,达到28.89%,同时改善了加热炉进料性质,从而可延长装置的运行周期.由于以煤沥青作为焦化的进料,其所产的焦炭符合石油焦1B的标准,可在炼铝工业中使用,从而提高了煤沥青的附加值,增加了煤焦油加工企业的经济效益.针对煤沥青焦化液体产品性质差的特点,应采用较高氢分压、较高反应温度和较低空速对其进行加氢处理.%The experiment of delayed coking of coal tar pitch has been performed at the selected conditions. The results showed that the liquid product yield of 10% to 20% could be achieved with the feed of coal tar pitch, and it could be greatly increased to 28. 89% with the coal tar pitch feed mixed with anthracene oil. The feed properties of heaters were improved and operating cycle of the unit was extended. As the coal tar pitch was used as the feed of delayed coker, the coke product met the 1B standard for petroleum coke, which could be used in aluminum industry. As the result, the added value of coal tar pitch was raised and the economic benefits of the company were improved. The liquid products from coal tar pitch coking should be hydro-treated at a higher hydrogen partial pressure, higher reactor temperature and lower space velocity because of the low quality.

  9. 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

  10. 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.

  11. 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.

  12. 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.

  13. 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.

  14. 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.

  15. 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)

  16. 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.

  17. 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)

  18. Assessment of coke oven emissions exposure among coking workers

    Energy Technology Data Exchange (ETDEWEB)

    Chen, M.L.; Mao, I.F.; Wu, M.T.; Chen, J.R.; Ho, C.K.; Smith, T.J.; Wypij, D.; Christiani, D.C. [National Yang Ming University, Taipei (Taiwan). Dept. of Public Health

    1999-01-01

    Coking workers are regularly exposed to coke oven emissions, which consist primarily of polycyclic aromatic hydrocarbons and volatile organic compounds. This study measured the workers` exposure to the benzene soluble fraction of total particulates (BSF). Personal breathing-zone samples of BSF and total particulates were taken from all study subjects for 3 consecutive days. The highest BSF concentrations were found among the topside oven workers. Among the samples at the topside oven 84% exceeded the Occupational Safety and Health Administration standard (150 {mu}g/m{sup 3} BSF). The percentage of BSF in total particulates varied across job classifications, ranging from 0.3% in wharf men to 24% in tar chasers. Area sampling indicated that the BSF concentration at the topside area was sixty fold higher than that at the administrative area, which was approximately 2 km from the coke oven plant.

  19. 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...

  20. 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

  1. 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.

  2. 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。

  3. 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

  4. 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

  5. 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...

  6. 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.

  7. 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.

  8. AN ELECTROLYTIC CIP-CLEANING PROCESS FOR REMOVING IMPURITIES FROM THE INNER SURFACE OF A METALLIC CONTAINER

    DEFF Research Database (Denmark)

    2008-01-01

    The invention relates to a novel electrolytic process for removing impurities from the inner surface of a metallic container. The process is particularly useful for cleaning process reactors used for culturing microorganisms, and storage tanks used for storing metabolites formed in the process...... reactor, as well as containers for dairy products....

  9. 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)

  10. 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)

  11. 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...

  12. A Research and Discussion on UHR Process in Advanced Treatment of Coking Wastewater%UHR工艺在深度处理焦化废水中的研究与探讨

    Institute of Scientific and Technical Information of China (English)

    龙泽勇

    2016-01-01

    The UHR process flow, characteristics and technical research on UHR advanced treatment of coking wastewater are introduced. Research results showed that UHR system operates very stably with good water quality, which fully meets national secondary discharge standard, and low COD and ammonia nitrogen content in the reverse osmosis concentrated water, which can satisfy the requirements of casting slag.%介绍了UHR工艺流程、特点及在深度处理焦化废水中的技术研究。研究表明:UHR系统运行十分稳定,出水水质良好,完全达到国家二级排放标准;反渗透浓水COD和氨氮含量小,能够满足浇渣的要求。

  13. 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。

  14. 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.

  15. 甲烷无氧芳构化反应器及催化剂积炭的研究进展%Process in Reactor and Catalyst Coke of Methane Dehydroaromatization Under the Condition of Oxyger Free

    Institute of Scientific and Technical Information of China (English)

    袁钊; 陆江银

    2012-01-01

    Concluded the research progress of non - oxidative aromatization of methane on the reaction mechanism, the choice of reactor and catalysts, catalyst coke and regeneration, which were significant in the fields of process development , energy utilization and catalysis science.%综述了甲烷无氧芳构化反应的研究进展,对甲烷无氧芳构化反应机理、反应器的选择、催化剂的选择、催化剂积炭失活与再生等方面做了讨论,对甲烷无氧芳构化的工艺开发、对能源利用、催化科学均具有重大意义。

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

    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.

  17. Chemical composition of coal and coke ash

    Energy Technology Data Exchange (ETDEWEB)

    Pluzhnikov, A.I.; Tsymbal, G.L.

    1983-05-01

    Karaganda Metals uses low sulphur coal from Karaganda and Kuzbass coalfields and is seeking ways of improving coke in terms of ash and its effect on blast furnace operations, chiefly coke rate reduction. Ash in coke has a critical effect on iron quality, slag composition and desulphurisation. The index used to demonstrate the change in coke consistency during incineration in the blast furnace is that of pyrolytic change: this closely reflects changes in coal charge composition. Control of coke ash content by suitably selecting the charge can be used to influence slag basicity and iron quality.

  18. 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

  19. 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.

  20. Practice of Advanced Treatment Process for Coking Wastewater in Bayuquan Company of Ansteel%鞍钢鲅鱼圈焦化废水深度处理工艺实践

    Institute of Scientific and Technical Information of China (English)

    张勇; 赵恒波; 杨大立; 孙大鹏

    2015-01-01

    针对鞍钢股份有限公司鲅鱼圈钢铁分公司焦化废水A2/O生物系统处理后出水COD、总氰及氨氮仍很难达标,生物处理段处理效果不好等问题,对臭氧催化氧化及电絮凝焦化废水深度处理工艺进行了研究。工业实践表明,将原A2/O生物系统出水经臭氧催化氧化深度处理后,COD和总氰化物去除率分别达到66%和84%,出水指标达到设计要求,环境效益显著。%The advanced treatment processes for coking wastewater based on the catalytic ozonation method and the electric coagulation method were studied with regard to the problems that the content of COD, total cyanide and ammonia nitrogen in effluent water obtained by the A2/O biological treatment system for coking wastewater in Bayuquan Iron &Steel Subsidiary Company of Angang Steel Co., Ltd. was far away from meeting the standard values and the treatment efficiency in biological treatment stage was not favorable. The practice shows that the removal rates of COD and total cyanide of effluent water which was obtained by the A2/O biological treatment system retreated by the advanced treatment process based on catalytic ozonation method were improved to 66% and 84% respectively and therefore indexes of effluent water can meet the values required by design standards while the environmental benefits are remarkable.

  1. 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.

  2. 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

  3. 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.

  4. 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...

  5. 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.

  6. 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

  7. 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)

  8. 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.

  9. Application of two-fluid nozzles for advanced photomask cleaning process

    Science.gov (United States)

    Masui, Kenji; Takemoto, Tetsuo; Otsubo, Kyo; Sakai, Mari; Higaki, Tomotaka; Watanabe, Hidehiro; Kikuchi, Tsutomu; Kurokawa, Yoshiaki

    2008-05-01

    Damage to minute features of 45nm-node device masks occurred during megasonic cleaning. Since we were obliged to weaken the mechanical effect of megasonics in order to prevent the collapse of minute features, we could not obtain acceptable cleaning results. In order to manage the minute features, there is a need to develop a new mechanical cleaning method that causes less damage, but does not compromise the ability to remove particles. Cleaning using a two-fluid nozzle is a promising candidate. We investigated the two-fluid nozzle and compared it with megasonic cleaning, and we confirmed that the two-fluid nozzle achieved acceptable cleaning results without damaging 45nm-node device masks. Furthermore, for 32nm-node device masks, we have improved the two-fluid nozzle in terms of the cleaning energy distribution.

  10. 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.

  11. 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

  12. 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.

  13. 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)

  14. 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.

  15. 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

  16. 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

  17. Preperation for a Clean Surface

    Directory of Open Access Journals (Sweden)

    Aurimas Ralys

    2013-02-01

    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

  18. 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...

  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. Improvement of Heat Exchanger Cleaning Process%热交换器在线清洗流程改进

    Institute of Scientific and Technical Information of China (English)

    蔡晓君; 尚彦芝; 刘湘晨; 张建军; 肖涤; 欧阳子劲; 张圆圆; 张文喜

    2012-01-01

    The cleaning of heat exchanger is an important part in industrial production, especially in oil chemical and thermoelectric factory production. So a simple cleaning process of heat exchanger for regular cleaning is very necessary. Based on the most basic online cleaning process and the test in the plant, a more practical, more concise and more convenient cleaning process will be put into application.%热交换器清洗是工业生产,尤其是石油化工及热电工厂生产中不可缺少的重要环节,采用简单可行的清洗流程对热交换器进行定期清洗很有必要.在最基本的在线清洗流程设计基础上,结合现场试验情况,通过不断改进,得到了更加实用、简洁、方便的清洗流程.

  1. DEVELOPING AN OPTIMIZED PROCESS STRATEGY FOR ACID CLEANING OF THE SAVANNAH RIVERSITE HLW TANKS

    Energy Technology Data Exchange (ETDEWEB)

    Ketusky, E

    2006-12-04

    At the Savannah River Site (SRS), there remains approximately 35 million gallons of High Level Waste (HLW) that was mostly created from Purex and SRS H-Area Modified (HM) nuclear fuel cycles. The waste is contained in approximately forty-nine tanks fabricated from commercially available carbon steel. In order to minimize general corrosion, the waste is maintained as very-alkaline solution. The very-alkaline chemistry has caused hydrated metal oxides to precipitate and form a sludge heel. Over the years, the sludge waste has aged, with some forming a hardened crust. To aid in the removal of the sludge heels from select tanks for closure the use of oxalic acid to dissolve the sludge is being investigated. Developing an optimized process strategy based on laboratory analyses would be prohibitively costly. This research, therefore, demonstrates that a chemical equilibrium based software program can be used to develop an optimized process strategy for oxalic acid cleaning of the HLW tanks based on estimating resultant chemistries, minimizing resultant oxalates sent to the evaporator, and minimizing resultant solids sent to the Defense Waste Processing Facility (DWPF).

  2. 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.

  3. 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

  4. 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.

  5. 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.

  6. 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.

  7. 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...

  8. 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...

  9. Effect of the surface properties of an activated coke on its desulphurization performance

    Institute of Scientific and Technical Information of China (English)

    ZHANG Xiang-lan; ZHANG Yan; DING Fang-sheng; HUANG Qi-jiang; LI Yuan

    2009-01-01

    Commercial coke was modified by H2O2 and/or NH3·H2O to obtain an activated coke containing additional oxygen func-tional groups and/or nitrogen functional groups. The aim of the modification was to enhance the SO2 adsorption capacity of the activated coke. Several techniques, including total nitrogen content measurements, SO2 adsorption, XPS and FTIR analysis, were used to characterize the coke samples. The XPS and FTIR spectra suggest the existence of-CONH2 groups in the H2O2 plus ammo-nia modified coke. The SO2 adsorption capacity of an activated coke increases slightly with an increase in H2O2 concentration dur-ing the modification process. The desulphurization performance of a modified coke is considerably enhanced by increasing the treatment temperature during ammonia modification. The amount of nitrogen in a coke modified by H2O2 plus NH3·H2O is the highest, and the SO2 adsorption capacity of the coke is also the highest (89.9 mg/gC). The NH3·H2O (only) modified sample has lower nitrogen content and lower desulphurization capacity (79.9 mg/gC). H2O modification gives the lowest SO2 adsorption capacity (28.9 mg/gC). The H2O2 pre-treatment is beneficial for the introduction of nitrogen onto the surface of a sample during the following ammonia treatment process.

  10. 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.

  11. 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

  12. 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.

  13. 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.

  14. 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...

  15. 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...

  16. 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.

  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 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...

  18. 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.

  19. 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.

  20. 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

  1. 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.

  2. Integration of natural pollutant retention and degradation processes in groundwater sanitation at LMBV MBH. The former Profen coking plant; Praxis der Einbindung von natuerlichem Schadstoffrueckhalt und -abbau in die Grundwasser-Sanierung der LMBV MBH. Am Beispiel der ehemaligen Schwelerei Profen

    Energy Technology Data Exchange (ETDEWEB)

    Thomas, A. [LMBV mbH, Ingenieurbereich Technik, Bitterfeld (Germany); Hahlbeck, S. [Staatliche Baumanagement Hannover II, Hannover (Germany)

    2005-07-01

    Using the example of the former Profen coking plant, practical experience is presented as follows: Description of the contamination situation and the relevant aspects of pollutant degradation; management of licenses for stopping active groundwater decontamination; experience in three years of monitoring after stopping active groundwater decontamination in April 2002; questions and problems concerning the applicability of the results to other contaminated sites and general conclusions concerning the integration of natural pollutant retention and degradation processes in sanitation measures. (orig.)

  3. 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, ...

  4. 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)

  5. Selection and Execution for Process Scheme of Synthetic Ammonia Made by Coke-Oven Gas%焦炉煤气制合成氨工艺方案的选取和实施

    Institute of Scientific and Technical Information of China (English)

    文德国; 苏庆贺; 陈世通

    2014-01-01

    介绍了山东临沂恒昌化工科技有限公司焦炉煤气制合成氨装置的立项背景;确定了装置的工艺方案和主要设备;简述了装置节能降耗的主要措施。结果表明:该装置一次试车成功,吨氨电耗约1000 kW· h,制造成本约1500元/t,经济效益明显。%Author has introduced the project approval background for plant of synthetic ammonia made by coke-oven gas in the Shandong Linyi Hengchang Chemical Engineering Science and Technology Company Ltd .; has determined the process scheme and main equipment; has described the main measures about energy saving and consume lowering.Result indicates that the trial run of plant was succesful in one time, the electricity power per ton of ammonia is saved by 1 000 kW· h, fabrication cost is saved by 1 500 Yuan RMB per ton, the economic benefit is obvious.

  6. 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.

  7. 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.

  8. 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.

  9. 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

  10. REINVESTIGATING THE PROCESS IMPACTS FROM OXALIC ACIDHIGH LEVEL WASTE TANK CLEANING

    Energy Technology Data Exchange (ETDEWEB)

    Ketusky, E

    2008-01-22

    The impacts and acceptability of using oxalic acid to clean the Savannah River Site, High Level Waste Tanks 1-8, were re-investigated using a two-phased approach. For the first phase, using a representative Tank 1-8 sludge, the chemical equilibrium based software, OLI ESP{copyright} and Savannah River Site laboratory test results were used to develop a chemically speciated material balance and a general oxalate mass balance. Using 8 wt% oxalic acid with a 100% molar excess, for every 1 kg of sludge solid that was dissolved, about 3.4 kg of resultant solids would form for eventual vitrification, while about 0.6 kg of soluble oxalate would precipitate in the evaporator system, and form a salt heel. Using available analyses, a list of potential safety and process impacts were developed, screened, and evaluated for acceptability. The results showed that the use of oxalic acid had two distinct types of impacts, those which were safety based and required potential upgrades or additional studies. Assuming such were performed and adequate, no further actions were required. The second type of impacts were also acceptable, but were long-term, and as such, would need to be managed. These impacts were directly caused by the solubility characteristics of oxalate in a concentrated sodium solution and, occurred after pH restoration. Since oxalate destruction methods are commonly available, their use should be considered. Using an oxalate destruction method could enable the benefits of oxalic to applied, while eliminating the long-term impacts that must be managed, and hence should be considered.

  11. 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。

  12. 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

  13. 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.

  14. Effect of coke strength on blast furnace performance

    Energy Technology Data Exchange (ETDEWEB)

    Belyshov, V.N.; Emushintsev, V.V.; Minikes, E.E.; Tsymbal, G.L.; Vakulin, V.N.

    1985-09-01

    The authors report on results of a study, conducted from 1979 to 1982, analyzing the effect of the strength of commercially produced coke on furnace performance, for furnaces of different volumes. The effect of coke strength on blast-furnace performance was analyzed in two directions: determination of the dependence of coke loss from fragmentation on coke strength indices; evaluation of the effect of the coke strength on melting indices. It is found that high-strength coke is needed for large-volume furnaces and that reduction in coke strength helps cause tuyere burning.

  15. 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.

  16. 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...

  17. 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.

  18. 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

  19. 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)

  20. 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

  1. 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...

  2. 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...

  3. 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%.

  4. 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.

  5. 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.

  6. 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.

  7. 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.

  8. 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.

  9. 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

  10. 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.

  11. 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...

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

    Energy Technology Data Exchange (ETDEWEB)

    Yokota, Yasuyuki; Hara, Hisaya; Morino, Yusuke; Bando, Ken-ichi; Imanishi, Akihito; Fukui, Ken-ichi, E-mail: kfukui@chem.es.osaka-u.ac.jp [Department of Materials Engineering Science, Graduate School of Engineering Science, Osaka University, 1-3 Machikaneyama, Toyonaka, Osaka 560-8531 (Japan); Uemura, Takafumi; Takeya, Jun, E-mail: takeya@k.u-tokyo.ac.jp [Department of Advanced Materials Science, Graduate School of Frontier Science, The University of Tokyo, 5-1-5 Kashiwa, Chiba 277-8561 (Japan); The Institute of Scientific and Industrial Research (ISIR), Osaka University, 8-1 Mihogaoka, Ibaraki, Osaka 567-0047 (Japan)

    2014-06-30

    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.

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

    Science.gov (United States)

    Yokota, Yasuyuki; Hara, Hisaya; Morino, Yusuke; Bando, Ken-ichi; Imanishi, Akihito; Uemura, Takafumi; Takeya, Jun; Fukui, Ken-ichi

    2014-06-01

    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.

  14. 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.

  15. An additive for a petroleum coke and water suspension

    Energy Technology Data Exchange (ETDEWEB)

    Khiguti, K.; Igarasi, T.; Isimura, Y.; Kharaguti, S.; Tsudzina, T.

    1983-03-04

    The patent covers an additive for a petroleum coke and watersuspension which contains soap of an aliphatic acid (AM) and or a salt of a maleic acid copolymer (SMK). The aliphatic acid soap is a salt of an alkaline earth metal of C6 to C22 aliphatic acid, an ammonium salt or a salt of a lower amine. The maleic acid copolymer is a salt (sodium, NH4) of a lower amine of a maleic anhydride copolymer with a copolymerizing vinyl additive. Capric acid, lauric acid, palmatic acid, aleic and other acids may be used as the aliphatic acid, while methylamine, trimethylamine, diethanolamine, morpholine and so on may be used as the lower amine salt. Ethylene, vinylchloride, methyl(meta)acrylate and so on are used as the polymerizing vinyl compound. The molar ratio of the maleic anhydride to the polymerizing vinyl compound is in a range from 1 to 1 to 1 to 10 (preferably 1 to 1 to 1 to 3). The maleic acid copolymer has a mean molecular mass within 1,000 to 5,000. The additive with the optimal composition contains a solvent, a thickener, an anticorrosion substance, anticoagulants, surfacants (PAV) and so on. A highly concentrated suspension of oil coke and water with a 50 to 75 percent concentration of powder form petroleum coke may be produced using the patented additive. Such a suspension is characterized by low viscosity, high stability and forms no foam during processing.

  16. 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.

  17. 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.

  18. 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.

  19. 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.

  20. 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

    (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 often encountered in the food industry. However, the extent to which PI is utilized is much smaller than the number of potential applications. The present paper will address this topic, give some reasons for the underuse of PI, and indicate some principles, methods, and directions that, when applied...

  1. 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.)

  2. 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.

  3. 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...

  4. Treatment of Refinery-Coking Wastewater by Aeration Micro-electrolysis Process with Hydrogen Peroxide%曝气微电解-双氧水工艺处理炼厂焦化废水

    Institute of Scientific and Technical Information of China (English)

    林伟帮; 李琪琪; 杨贺群; 谭毅; 蒋伟芬; 陈英; 陈东

    2012-01-01

    The rcfinery-coking wastewater was treated by aeration micro-electrolysis process with hydrogen peroxide. The influence of pH, reaction time, hydrogen peroxide and Iron filings dosage, and air flow on the removal of COD and NH3-N, and the ratio of BOD and COD for the waste water was investigated. The removal of COD and NH3-N in the wastewater was 37.6 % and 29.9 % respectively under the conditions of pH 5-7, Iron filings dosage of 100 g/L, hydrogen peroxide (30 % concentration)dosage of 2 mL/L, and 60 L/h air flow per 150 mL wastewater after reaction 90 rain. The ratio of BOD and COD increased from 0.25 to 0.66, which implied that the biodegradability of the wastewater was improved.%采用曝气微电解-双氧水工艺处理炼厂焦化废水,考察了废水pH、反应时间、双氧水投加量以及空气流量等因素对废水COD、NH3-N2、除率和BOD/COD比值的影响。结果表明,在pH5~7、铁稻用量100g/L、双氧水(浓度为30%)用量2mL/L,反应时间1.5h、空气流量60L/h(实验废水量150mL)的条件下,COD、NH3-N的去除率分别为37.6%和299%,BOD/COD比值从0.25提高到0.66,废水可生化性提高。

  5. 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...

  6. 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)

  7. Shortcut Nitrification/Anaerobic Ammonium Oxidation/Complete Nitrification Process for Treatment of Coking Wastewater%短程硝化/厌氧氨氧化/全程硝化工艺处理焦化废水

    Institute of Scientific and Technical Information of China (English)

    薛占强; 李玉平; 李海波; 林琳; 曹宏斌

    2011-01-01

    通过对短程硝化和厌氧氨氧化工艺的研究,开发了短程硝化/厌氧氨氧化/全程硝化(O1/A/O2)生物脱氮新工艺并用于焦化废水的处理.控制温度为(35±1)℃、DO为2.0~3.0mg/L,第一级好氧连续流生物膜反应器在去除大部分有机污染物的同时还实现了短程硝化.考察了HRT、DO和容积负荷对反应器运行效果的影响.结果表明,当氨氮容积负荷为0.13~0.22gNH4+-N/(L·d)时,连续流反应器能实现短程硝化并有效去除氨氮.通过控制一级好氧反应器的工艺参数,为厌氧反应器实现厌氧氨氧化(ANAMMOX)创造条件.结果表明,在温度为34℃、pH值为7.5~8.5、HRT为33 h的条件下,经过115 d成功启动了厌氧氨氧化反应器.在进水氨氮、亚硝态氮浓度分别为80和90 mg/L左右、总氮负荷为160 mg/(L·d)时,对氨氮和亚硝态氮的去除率最高分别达86%和98%,对总氮的去除率为75%.最后在二级好氧反应器实现氨氮的全程硝化,进一步去除焦化废水中残留的氨氯、亚硝态氮和有机物.O1/A/O2工艺能有效去除焦化废水中的氨氮和有机物等污染物,正常运行条件下的出水氨氮<15 mg/L、亚硝态氮<1.0 mg/L,COD降至124~186 mg/L,出水水质优于A/O生物脱氮工艺的出水水质.%The combined process of shortcut nitrification, anaerobic ammonium oxidation and complete nitrification was developed for the treatment of coking wastewater. The organic pollutants are mainly removed, and shortcut nitrification is obtained in the first-stage aerobic continuous-flow biofilm reactor at temperature of (35 ± 1 ) ℃ and DO of 2.0 to 3.0 mg/L. The effects of HRT, DO and volume load on the operation efficiency of the reactor were investigated. The results show that the shortcut nitrification is obtained, and ammonia nitrogen is effectively removed in the reactor. The process parameters of the reactor are controlled to achieve anaerobic ammonium oxidation in the anaerobic reactor

  8. Preliminary Study of Thermal Treatment of Coke Wastewater Sludge Using Plasma Torch

    Science.gov (United States)

    Li, Mingshu; Li, Shengli; Sun, Demao; Liu, Xin; Feng, Qiubao

    2016-10-01

    Thermal plasma was applied for the treatment of coke wastewater sludge derived from the steel industry in order to investigate the feasibility of the safe treatment and energy recovery of the sludge. A 30 kW plasma torch system was applied to study the vitrification and gas production of coke wastewater sludge. Toxicity leaching results indicated that the sludge treated via the thermal plasma process converted into a vitrified slag which resisted the leaching of heavy metals. CO2 was utilized as working gas to study the production and heat energy of the syngas. The heating value of the gas products by thermal plasma achieved 8.43 kJ/L, indicating the further utilization of the gas products. Considering the utilization of the syngas and recovery heat from the gas products, the estimated treatment cost of coke wastewater sludge via plasma torch was about 0.98 CNY/kg sludge in the experiment. By preliminary economic analysis, the dehydration cost takes an important part of the total sludge treatment cost. The treatment cost of the coke wastewater sludge with 50 wt.% moisture was calculated to be about 1.45 CNY/kg sludge dry basis. The treatment cost of the coke wastewater sludge could be effectively controlled by decreasing the water content of the sludge. These findings suggest that an economic dewatering pretreatment method could be combined to cut the total treatment cost in an actual treatment process.

  9. 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.

  10. 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.

  11. 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.

  12. 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.

  13. Study and Design on Cleaning Process of Oil Drum%油桶清洗工艺研究与设计

    Institute of Scientific and Technical Information of China (English)

    徐斌; 祝秀琴

    2012-01-01

    Used oil barrel should be cleaned and dried before using again.This paper gives a new cleaning process based on the study of cleaning theory and the dirty of the oil drum's inner face.%旧油桶重新投入使用前,必须对油桶进行清洗及干燥。本文通过对清洗原理及待洗油桶内部油垢状况的研究,提出了一种油桶的清洗工艺流程。

  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. 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。

  16. 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 ...

  17. 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.

  18. 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

  19. 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.

  20. 干熄焦炉内三维流动及传热的数值模拟%3D numerical simulation of flow and heat transfer in coke dry quenching process

    Institute of Scientific and Technical Information of China (English)

    常庆明; 靳振伟; 程平平; 李亚伟; 董良君

    2014-01-01

    A mathematical model for quenching gas flow and heat transfer between gas and coke in the coke dry quenching (CDQ) unit was established .In the model ,secondary development was done on the platform of Fluent by employing the user defined functions (UDF) and the user defined scalars (UDS) .The calculation results show a bias flow of quenching gas in the chutes ,i .e .more gas flows to the annular gas passage through the chutes near the outlet with relatively larger velocity .The pres-sure loss of the flowing gas mainly takes place in the cooling chamber ,and the heat transfer rate be-tween gas and coke near the side in the chamber is larger than that at the center .Simulation results find that the heated gas temperature can reach about 1101 K at the gas outlet w hile the cooled coke temperature decreases to about 439 K at the coke outlet w hen the circulating air volume is 200 000 m3/h .This can not only meet the cooling requirement of the coke but also supply the recycle gas with high grade heat for further heating or power generation .%以Fluent软件为平台,通过流体在多孔介质中的流动模型来处理冷却气体在干熄焦炉内的三维流动,借助于UDS和UDF进行二次开发,建立干熄焦炉内冷却气体及焦炭的流动传热模型,并分析了循环风量对气固换热的影响。结果表明,冷却室气体在通过斜道进入环形气道时有偏流现象,即靠近总出口附近的斜道有更多的气体流出,且气流速度最快;气体的压力损失主要发生在冷却室;冷却室内周边的换热效果比中心换热效果要好。模拟计算发现,循环风量为200000 m3/h时,换热后的冷却气体温度为1101 K ,焦炭温度为439 K ,这不仅满足了焦炭的冷却要求,而且还能提供用于供暖或发电的高品位热量的循环气体。

  1. 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).

  2. Study on the recovery process of hydrocarbon cleaning agent%碳氢清洗剂再生利用工艺方法的研究

    Institute of Scientific and Technical Information of China (English)

    刘瑞广

    2011-01-01

    ODS(Ozone Depleting Substances) cleaning agent takes a large portion in halogenated cleaning agent, which is the most common cleaning agent. The use of halogenated cleaning agent has threatened human, object to be cleaned and the environment. As a substitute of halogenated cleaning agent, hydrocarbon cleaning agent has been widely used in the recent years. Compared with halogenated cleaning agent, hydrocarbon cleaning agent has higher boiling point 150-190 ℃ and lower flashing point 50~70 ℃, which means the traditional cleaning agent recovery process are not suitable to recover hydrocarbon cleaning agent. This paper describes a new method to recover hydrocarbon cleaning a-gent. The recovery process is sulfuric acid extraction, clarification and distillation. Thus, the final product is qualified to be reused, and the sulfuric acid can also be reused.%在工业清洗领域使用最多的卤代烃清洗剂,其中ODS(破坏臭氧层物质)清洗剂占有很大比重,但在使用中对人、被清洗物和环境会带来许多危害.为此,各种替代产品和替代技术应运而生.从经济、适用、安全、环保等方面综合评价,经过多年的探索、论证、比较和筛选,碳氢清洗剂作为替代品已得到广泛应用,尽管碳氢清洗剂有诸多优点,但与ODS清洗剂相比,其沸点高(150~190℃)、闪点低(50~70℃)、与被清洗的物质相容性好,使碳氢清洗剂的再生无法用原有工艺方法实现.本工艺方法的研究是采取硫酸萃取、静置分离、精馏的方法再生碳氢清洗剂,达到原有的品质重复利用,硫酸萃取剂蒸馏回收重复利用,达到资源化利用的目的.

  3. 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...

  4. Construction solutions applied at coke oven battery no. 7 in the aspect of international requirements

    Energy Technology Data Exchange (ETDEWEB)

    Tadeusz Maj; Mariola Honisz; Wladyslaw Latocha; Wiktor Humer; Ludwik Kosyrczyk [' Zdzieszowice' Coking Plant Ltd. (Poland)

    2004-07-01

    15 slides/overheads outline this presentation. In February 2003 a new coke oven battery was put into operation in Zdzieszowice. In view of Poland's joining the European Union a series of technical solutions were implemented to improve working conditions in addition to improving the technology of the coking process. The paper describes the actions taken over one and a half years of operation. These include maintaining the recommended low level of NOx emission (comparable to that of CO) by waste gas recirculation.

  5. Chemical composition of ash in coal and coke

    Energy Technology Data Exchange (ETDEWEB)

    Pluzhnikov, A.I.; Tsymbal, G.L.

    1983-05-01

    Ash content in coke influences coke consumption rate by blast furnaces. In the Karaganda steelworks a 1% ash content decrease in coke reduces coke consumption by a blast furnace by 1 to 1.6%. Ash content in coke depends on ash content in a coal mixture and ash content in a coal mixture depends on ash content and washability of coal components. Not all ash components are of identical importance for blast furnace coke production. Investigations show that silica and aluminium oxides are only slightly influenced by thermal degradation and reduction reactions which take place during coking. Coal pyrolysis decisively influences content of sodium oxides, potassium oxides or iron oxides. Sodium and potassium carbonates are also unstable and undergo degradation. Taking into consideration that silica and aluminium oxides are not influenced by thermal degradation during coking an increase in the two oxides in a coal mixture used for coking causes an ash content increase in coke. Examples of coal from the Kuzbass and the Vorkuta mines are given. Replacing 5% of the KZh and K coal from Karaganda with G6 coal from the Kuzbass characterized by the identical ash content but by higher content of silica and aluminium oxides causes an increase in ash content in coke ranging from 1.6 to 1.8%. (8 refs.)

  6. 77 FR 32998 - Foundry Coke From China

    Science.gov (United States)

    2012-06-04

    ... The Commission instituted this review on December 1, 2011 (76 FR 74810) and determined on March 5, 2012 that it would conduct an expedited review (77 FR 15123, March 14, 2012). The Commission... COMMISSION Foundry Coke From China Determination On the basis of the record \\1\\ developed in the subject...

  7. 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

  8. 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.

  9. [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

  10. 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.

  11. 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。

  12. 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

  13. Investigation into environmentally friendly alternative cleaning processes for hybrid microcircuits to replace vapor degreasing with 1,1,1-trichloroethane. Final report

    Energy Technology Data Exchange (ETDEWEB)

    Adams, B.E.

    1997-02-01

    Two cleaning processes, one aqueous and one nonaqueous, were investigated as potential replacements for the vapor degreasing process using 1,1,1 trichloroethane (TCA) for hybrid microcircuit assemblies. The aqueous process was based upon saponification chemistry. A 10% solution of either Kester 5768 or Armakleen 2001, heated to 140 F, was sprayed on the hybrid at 450 psig and a flow rate of 5 gpm through a specially designed nozzle which created microdroplets. The nonaqueous process was based upon dissolution chemistry and used d-limonene as the solvent in an immersion and spray process. The d-limonene solvent was followed by an isopropyl alcohol spray rinse to remove the excess d-limonene. The aqueous microdroplet process was found to be successful only for solder reflow profiles that did not exceed 210 C. Furthermore, removal of component marking was a problem and the spray pressure had to be reduced to 130 psig to eliminate damage to capacitor end caps. The d-limonene cleaning was found to be successful for solder reflow temperature up to 250 C when using a four-step cleaning process. The four steps included refluxing the hybrid at 80 C, followed by soaking the hybrid in d-limonene which is heated to 80 C, followed by spray cleaning at 80 psig with room temperature d-limonene, followed by spray cleaning at 80 psig with room temperature IPA was developed to remove residual flux from the hybrid microcircuits. This process was the most robust and most closely matched the cleaning ability of TCA.

  14. 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.

  15. A new multiple-stage electrocoagulation process on anaerobic digestion effluent to simultaneously reclaim water and clean up biogas.

    Science.gov (United States)

    Liu, Zhiguo; Stromberg, David; Liu, Xuming; Liao, Wei; Liu, Yan

    2015-03-21

    A new multiple-stage treatment process was developed via integrating electrocoagulation with biogas pumping to simultaneously reclaim anaerobic digestion effluent and clean up biogas. The 1st stage of electrocoagulation treatment under the preferred reaction condition led to removal efficiencies of 30%, 81%, 37% and >99.9% for total solids, chemical oxygen demand, total nitrogen and total phosphorus, respectively. Raw biogas was then used as a reactant and pumped into the effluent to simultaneously neutralize pH of the effluent and remove H2S in the biogas. The 2nd stage of electrocoagulation treatment on the neutralized effluent showed that under the selected reaction condition, additional 60% and 10% of turbidity and chemical oxygen demand were further removed. The study concluded a dual-purpose approach for the first time to synergistically combine biogas purification and water reclamation for anaerobic digestion system, which well addresses the downstream challenges of anaerobic digestion technology.

  16. 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。

  17. 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.)

  18. 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

  19. 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.

  20. 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...

  1. High-porosity permeable cellular metals and alloys in catalytic processes of gas cleaning

    Energy Technology Data Exchange (ETDEWEB)

    Antsiferov, V.N.; Makarov, A.M.; Khramtsov, V.D. [Research Center of Powder Material Engineering, Perm (Russian Federation)

    2005-01-01

    During the rotational moulding of plastics there are a number of key temperatures that influence to a large extent the production of good quality parts. Using well established relationships between the structure and processibility of plastics, this paper explains why polyethylene is much easier to process by rotational moulding than other polymers such as polyamides, poly(ethylene terephtalate), poly(vinylchloride) or polypropylene. (Abstract Copyright [2005], Wiley Periodicals, Inc.)

  2. Preliminary study into the effects of YAG laser processing of titanium 6Al-4V alloy for potential aerospace component cleaning application

    Energy Technology Data Exchange (ETDEWEB)

    Turner, M.W. [Rolls-Royce Compression Systems, Rolls Royce plc, P.O. Box 3, Skipton Road, Barnoldswick, Lancashire BB18 5RU (United Kingdom); Schmidt, M.J.J. [Rolls-Royce Compression Systems, Rolls Royce plc, P.O. Box 3, Skipton Road, Barnoldswick, Lancashire BB18 5RU (United Kingdom); Laser Processing Research Centre, Department of Mechanical, Aerospace and Manufacturing Engineering, University of Manchester Institute of Science and Technology (UMIST), Sackville Street, Manchester M60 1QD (United Kingdom); Li, L. [Rolls-Royce Compression Systems, Rolls Royce plc, P.O. Box 3, Skipton Road, Barnoldswick, Lancashire BB18 5RU (United Kingdom); Laser Processing Research Centre, Department of Mechanical, Aerospace and Manufacturing Engineering, University of Manchester Institute of Science and Technology (UMIST), Sackville Street, Manchester M60 1QD (United Kingdom)

    2005-07-15

    This paper outlines some essential gas turbine aeroengine component manufacture cleaning requirements. It describes the preliminary results of work conducted into the effects of laser processing Ti-6A-4V alloy for cleaning of aerospace components, including determination of the melt and surface coupling thresholds for the Nd:YAG ({lambda} = 1.064 {mu}m) system in use. The results of laser processing as a preparation for electron beam welding and diffusion bonding are presented. Finally, the direction of future work towards the development of an effective process for laser cleaning titanium aero-engine components is discussed. The results demonstrated the sensitivity of the system in use to gaseous contamination, producing acceptable electron beam welded joints, but unacceptable diffusion bonded joints.

  3. 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.

  4. Shift from coke to coal using direct reduction method and challenges

    Energy Technology Data Exchange (ETDEWEB)

    Okonkwo Paul Chukwuleke; Jiu-ju Cai; Sam Chukwujekwu; Song Xiao [Deakin University, Waurn Ponds, Vic. (Australia)

    2009-03-15

    Ironmaking involves the separation of iron ores. It not only represents the first step in steelmaking but also is the most capital-intensive and energy-intensive process in the production of steel. The main route for producing iron for steelmaking is to use the blast furnace, which uses metallurgical coke as the reductant. Concerns over the limited resources, the high cost of coking coals, and the environmental impacts of coking and sinter plants have driven steelmakers to develop alternative ironmaking processes that can use non-coking coals to reduce iron ores directly. Since the efficiency and productivity of modern large capacity blast furnaces will be difficult to surpass, blast furnaces will continue to retain their predominant position as the foremost ironmaking process for some time to come. The alternative ironmaking processes are therefore expected to play an increasingly significant role in the iron and steel industry, especially in meeting the needs of small-sized local and regional markets. It is likely that the importance of direct reduced iron (DRI) and hot metal as sources of virgin iron will continue to increase, especially in the developing countries where steelmaking is, and will be, primarily based on electric arc furnace (EAF) minimills. Consequently, the challenges that are faced by the new technology have to be embraced.

  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. 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.

  7. 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

  8. Understanding Particle Defect Transport in an Ultra-Clean Sputter Coating Process

    Energy Technology Data Exchange (ETDEWEB)

    Walton, C; Kearney, P; Folta, J; Sweeney, D; Mirkarimi, P

    2003-03-24

    Low-defect mask blanks remain a key technical challenge to Extreme Ultraviolet Lithography (EUVL). The mask blank is ion-beam sputter-coated with an 81-layer Mo/Si multilayer stack for high reflectance at {lambda} = 13.4nm. The current mask coating process can achieve a median added defect level of 0.05 defects/cm{sup 2} (12 added defects 90nm or larger on a 200mm Si-wafer test substrate), but this must be reduced by about a factor of 10 to meet mask cost requirements for EUVL. To further reduce the particle defect level, we have studied pathways for particle transport, using test particles and particles native to the coating process, and combined the results into a computational model of particle transport in an ion-beam sputter system. At process pressure, gas drag is negligible for particles above 100nm, so particles travel ballistically until they hit a surface. Bounce from chamber walls allows particles to reach all surfaces in the chamber if they have initial velocities above {approx}100m/s. The ion beam has sufficient momentum to entrain slower particles and accelerate them toward the sputter target, where some can bounce to the substrate. The model shows preliminary agreement with experimental defect distributions on witness wafers at various positions within the coating chamber.

  9. 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.

  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.

  11. 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.

  12. 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.

  13. 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

  14. 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...

  15. 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...

  16. 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.

  17. 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.

  18. 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

  19. 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

  20. 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...

  1. 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.

  2. 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...

  3. 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...

  4. 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.

  5. 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.

  6. A novel approach to mitigating sulphur dioxide emissions and producing a mercury sorbent material using oil-sands fluid coke

    Energy Technology Data Exchange (ETDEWEB)

    Morris, E.; Jia, C.Q. [Toronto Univ., ON (Canada). Dept. of Chemical Engineering and Applied Chemistry; Tong, S. [Wuhan Univ. of Science and Technology, Wuhan (China). Dept. of Chemical Engineering

    2008-07-01

    Pyrometallurgical smelting operations are a major source of sulphur dioxide (SO{sub 2}) 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 SO{sub 2} 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 SO{sub 2} emissions while producing elemental sulphur as well as coke-SO{sub 2}-oxygen (O{sub 2}) and coke-SO{sub 2}-water (H{sub 2}O) 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 SO{sub 2} and activation of fluid coke. It was concluded that more work is still needed to analyse the effect of O{sub 2} and SO{sub 2} reduction and SIAC properties under smelter flue gas conditions. 10 refs., 1 tab., 8 figs.

  7. 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.

  8. 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)

  9. 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

  10. 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.

  11. 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.

  12. 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.

  13. Reduction in toxicity of coking wastewater to aquatic organisms by vertical tubular biological reactor.

    Science.gov (United States)

    Zhou, Siyun; Watanabe, Haruna; Wei, Chang; Wang, Dongzhou; Zhou, Jiti; Tatarazako, Norihisa; Masunaga, Shigeki; Zhang, Ying

    2015-05-01

    We conducted a battery of toxicity tests using photo bacterium, algae, crustacean and fish to evaluate acute toxicity profile of coking wastewater, and to evaluate the performance of a novel wastewater treatment process, vertical tubular biological reactor (VTBR), in the removal of toxicity and certain chemical pollutants. A laboratory scale VTBR system was set up to treat industrial coking wastewater, and investigated both chemicals removal efficiency and acute bio-toxicity to aquatic organisms. The results showed that chemical oxygen demand (COD) and phenol reductions by VTBR were approximately 93% and 100%, respectively. VTBR also reduced the acute toxicity of coking wastewater significantly: Toxicity Unit (TU) decreased from 21.2 to 0.4 for Photobacterium phosphoreum, from 9.5 to 0.6 for Isochrysis galbana, from 31.9 to 1.3 for Daphnia magna, and from 30.0 to nearly 0 for Danio rerio. VTBR is an efficient treatment method for the removal of chemical pollutants and acute bio-toxicity from coking wastewater.

  14. 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

  15. PLUTONIUM CLEANING PROCESS

    Science.gov (United States)

    Kolodney, M.

    1959-12-01

    A method is described for rapidly removing iron, nickel, and zinc coatings from plutonium objects while simultaneously rendering the plutonium object passive. The method consists of immersing the coated plutonium object in an aqueous acid solution containing a substantial concentration of nitrate ions, such as fuming nitric acid.

  16. 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。

  17. 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

  18. 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.

  19. 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.

  20. 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

  1. 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...

  2. 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...

  3. 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.

  4. 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...

  5. 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)

  6. 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。

  7. 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...

  8. 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.

  9. 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)

  10. 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%.

  11. 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

    2016-08-01

    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.

  12. 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.

  13. 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.

  14. DuPont IsoTherming clean fuel technology

    Energy Technology Data Exchange (ETDEWEB)

    Levinski, E. [E.I. DuPont Co., Wilmington, DE (United States)

    2009-07-01

    This poster described a hydroprocessing technology that DuPont has acquired from Process Dynamics, Inc. The IsoTherming clean fuel technology significantly reduces sulphur in motor fuels. The technology provides petroleum refiners the solution for meeting ultra low sulphur diesel requirements, at much lower costs than conventional technologies. IsoTherming hydroprocessing operates in a kinetically limited mode, with no mass transfer limitation. Hydrogen is delivered to the reactor in the liquid phase as soluble hydrogen, allowing for much higher space velocities than conventional hydrotreating reactors. Treated diesel is recycled back to the inlet of the reactor, generating less heat and more hydrogen into the reactor. The process results in a more isothermal reactor operation that allows for better yields, fewer light ends and greater catalyst life. The technology reduces coking, because the process provides enough hydrogen in the solution when cracking reactions take place. As a result, the process yields longer catalyst life. Other advantages for refiners include lower total investment; reduced equipment delivery lead times; reduced maintenance and operating costs; and configuration flexibility. tabs., figs.

  15. 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.)

  16. Enhanced magnetic cleaning in magnetic enhanced flocculation membrane filtration process%磁絮凝膜过滤工艺中附加磁场强化清洗

    Institute of Scientific and Technical Information of China (English)

    王捷; 杨军; 贾辉; 张宏伟

    2014-01-01

    基于磁强化絮凝膜过滤(MEFMF)工艺中磁絮体和含磁滤饼层的特性,设计了在线(on-line)和离线(off-line)磁强化清洗(MEC)工艺。在磁场和曝气剪切的协同作用下,含磁滤饼层脱离膜纤维表面,膜通量恢复率较常规物理清洗(RC)明显提高。在离线磁强化清洗时,设计反洗装置中心的磁感应强度为6 mT,曝气强度为500 L·m−2·min−1,控制清洗时间为5 min,维持反洗压力0.04 MPa,可达到最佳的膜清洗效果,通量恢复率达97%以上。在外加磁场强化清洗过程中,滤饼层中的磁种发生磁化作用,滤饼层表现出微弱的宏观磁性,在磁场的作用下向磁极运动,使得膜通量恢复率明显提高。此外,在MEFMF工艺中采用间歇磁强化清洗,可以更加有效地去除引起不可逆膜污染的胶体和有机物,降低膜污染速率,减缓膜污染。%On the basis of the characteristics of magnetic flocs and cake layer in the magnetic enhanced flocculation membrane filtration (MEFMF) process, processes of on-line and off-line magnetic enhanced cleaning (MEC) were designed. Magnetic cake layer was separated from fiber surface under the synergistic effect of magnetic field force and aeration shear force, in which way the goal of optimization of membrane cleaning was achieved. The magnetic enhanced cleaning process was added to magnetic enhanced flocculation membrane filtration for off-line cleaning of fouled membrane module in MEFMF process. In the magnetic cleaning process with device’s magnetic induction 6 mT, aeration intensity 500 L·m−2·min−1, washing time to 5 min, backwash pressure 0.04 MPa, optimum cleaning effect could be achieved for flux recovery rate over 97%. In the enhanced cleaning process with magnetic field the magnetic seeding in the cake layer was magnetized, rendering the cake layer weak macro magnetism. Under the effect of the attached magnetic field the magnetized cake

  17. 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...

  18. 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.

  19. 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

  20. Coke Formation in a Zeolite Crystal During the Methanol-to-Hydrocarbons Reaction as Studied with Atom Probe Tomography.

    Science.gov (United States)

    Schmidt, Joel E; Poplawsky, Jonathan D; Mazumder, Baishakhi; Attila, Özgün; Fu, Donglong; de Winter, D A Matthijs; Meirer, Florian; Bare, Simon R; Weckhuysen, Bert M

    2016-09-01

    Understanding the formation of carbon deposits in zeolites is vital to developing new, superior materials for various applications, including oil and gas conversion processes. Herein, atom probe tomography (APT) has been used to spatially resolve the 3D compositional changes at the sub-nm length scale in a single zeolite ZSM-5 crystal, which has been partially deactivated by the methanol-to-hydrocarbons reaction using (13) C-labeled methanol. The results reveal the formation of coke in agglomerates that span length scales from tens of nanometers to atomic clusters with a median size of 30-60 (13) C atoms. These clusters correlate with local increases in Brønsted acid site density, demonstrating that the formation of the first deactivating coke precursor molecules occurs in nanoscopic regions enriched in aluminum. This nanoscale correlation underscores the importance of carefully engineering materials to suppress detrimental coke formation.

  1. Coke Formation in a Zeolite Crystal During the Methanol-to-Hydrocarbons Reaction as Studied with Atom Probe Tomography.

    Science.gov (United States)

    Schmidt, Joel E; Poplawsky, Jonathan D; Mazumder, Baishakhi; Attila, Özgün; Fu, Donglong; de Winter, D A Matthijs; Meirer, Florian; Bare, Simon R; Weckhuysen, Bert M

    2016-09-01

    Understanding the formation of carbon deposits in zeolites is vital to developing new, superior materials for various applications, including oil and gas conversion processes. Herein, atom probe tomography (APT) has been used to spatially resolve the 3D compositional changes at the sub-nm length scale in a single zeolite ZSM-5 crystal, which has been partially deactivated by the methanol-to-hydrocarbons reaction using (13) C-labeled methanol. The results reveal the formation of coke in agglomerates that span length scales from tens of nanometers to atomic clusters with a median size of 30-60 (13) C atoms. These clusters correlate with local increases in Brønsted acid site density, demonstrating that the formation of the first deactivating coke precursor molecules occurs in nanoscopic regions enriched in aluminum. This nanoscale correlation underscores the importance of carefully engineering materials to suppress detrimental coke formation. PMID:27485276

  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. 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.

  4. 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...

  5. 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.

  6. 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...

  7. 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.

  8. 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.

  9. 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.

  10. 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)

  11. 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.

  12. STUDY ON MICROTEXTURE OF COKE PRODUCED FROM CONVERTING LIGNITE BY USING CARBON MONOXIDE AND WATER

    Institute of Scientific and Technical Information of China (English)

    王洁; 郭黔杰

    1992-01-01

    Lignite,generally containing high levels of side chains and oxyfunctional groups,cannot lead to the formation of ordered coke texture. Changes in the properties of the lack of plasticity and fluidity during carbonization using a mixture of carbon monoxide and water conversion process were studied by the microscope photometry,by plotting Rmnx values against Rm,Rmin and bireflectance, as well as quantitative estimation of the optical anisotropy, based on 500 pointcounts. The classification of the carbon forms of this converted lignite is proposed as follows: Isotropic ,Mosaic ,Fibrous ,Flow & Leaf,Mesophase-sphere ,Fusitic ,Inertic ,Pore & fissure. This microtextures of coke were also analysed by using X-ray diffraction. It reveals that the values of diffractional angle,interlayer spacing (002) and the height of the crystallite are in good relationship with the degree of polymerization from the original lignite to its water gas shift reaction products.

  13. 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.

  14. 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)

  15. 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.

  16. 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

  17. 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...

  18. [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

  19. RESIDUA UPGRADING EFFICIENCY IMPROVEMENT MODELS: WRI COKING INDEXES

    Energy Technology Data Exchange (ETDEWEB)

    John F. Schabron; Joseph F. Rovani, Jr.; Francis P. Miknis; Thomas F. Turner

    2003-06-01

    Pyrolysis experiments were conducted with three residua at 400 C (752 F) at various residence times. The wt % coke and gaseous products were measured for the product oils. The Western Research Institute (WRI) Coking Indexes were determined for the product oils. Measurements were made using techniques that might correlate with the Coking Indexes. These included spin-echo proton nuclear magnetic resonance spectroscopy, heat capacity measurements at 280 C (536 F), and ultrasonic attenuation. The two immiscible liquid phases that form once coke formation begins were isolated and characterized for a Boscan residuum pyrolyzed at 400 C (752 F) for 55 minutes. These materials were analyzed for elemental composition (CHNS), porphyrins, and metals (Ni,V) content.

  20. Mineral matter in coals and their reactions during coking

    Energy Technology Data Exchange (ETDEWEB)

    Grigore, Mihaela; French, David [The Commonwealth Scientific and Industrial Research Organisation (CSIRO) - Energy Technology, Lucas Heights, NSW 2234 (Australia); Sakurovs, Richard [The Commonwealth Scientific and Industrial Research Organisation (CSIRO) - Energy Technology, Newcastle, NSW 2300 (Australia); Sahajwalla, Veena [School of Materials Science and Engineering, The University of New South Wales, Sydney, NSW 2052 (Australia)

    2008-12-01

    Degradation of coke in the blast furnace is influenced by its inherent mineral matter, the formation of which is itself dependent upon the nature of the coal mineral matter. To date few studies have been made of coke mineralogy and its relationship to the mineralogy of the parent coal. In this study the effect of carbonisation on coal mineral matter has been investigated by a detailed quantitative mineralogical examination of nine cokes and their parent coals. The quantitative analysis was performed on X-ray diffraction patterns of the mineral matter of cokes and coals, using SIROQUANT {sup trademark}. Coke mineralogy and its composition varied strongly between cokes, more strongly than variations in elemental composition of the ash. The mineral matter in the studied cokes consisted of crystalline mineral phases and also significant levels of amorphous phase (ranging between 44 and 75%). Decomposition of clays such as kaolinite, montmorillonite, illite and chamosite produced the amorphous phase and some of the crystalline mineral phases such as mullite, {gamma}-alumina, spinel, cristobalite and leucite. The type of association of mineral matter in coals had an important role in how the clays decomposed. For example, association of kaolinite with silica-bearing minerals in intimate intermixture favoured formation of mullite over {gamma}-alumina. Akermanite and diopside result from reaction of kaolinite with associated calcium bearing minerals (calcite, dolomite or ankerite). Quartz, fluorapatite and the three polymorphs of TiO{sub 2} (anatase, brookite and rutile) were the coal minerals that were least affected during carbonisation, as they were also found in the cokes, yet even they were affected in some cases. (author)

  1. Use of thermogravimetry for proximate analysis of coals and cokes

    Energy Technology Data Exchange (ETDEWEB)

    Ottaway, M.

    1982-08-01

    An alternative method for the proximate analysis of coals and cokes using a thermobalance is described. The test measures water content, volatile matter, fixed carbon, and ash residue and takes <10 min to complete. The variety of coals and cokes tested in this investigation have given results which showed good correlation with values from the prescribed method. The thermogravimetric technique appears to be a feasible rapid alternative to standard methods for proximate analysis. (11 refs.)

  2. 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...

  3. 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...

  4. 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.

  5. 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.

  6. Current status of patent technologies of coke oven gas to natural gas in China%国内焦炉气制天然气专利技术发展现状

    Institute of Scientific and Technical Information of China (English)

    杜雄伟

    2012-01-01

    Current status of patent technologies of coke oven gas to natural gas in China is described in this paper. Two main production processes of coke oven gas to natural gas are analyzed, named " coke oven gas methanation to natural gas" process and "coke oven gas purification and separation to natural gas" process. Patent applications of conversion technologies from coke oven gas to natural gas by organizations or individuals who have the technologies in China are introduced. It is pointed out that the project implementation of coke oven gas to natural gas has a very important significance for coking industry to develop energy-saving and emission-reduction circular economy.%综述了国内焦炉气制天然气专利技术发展现状,分析了国内焦炉气制天然气技术的2种主要工艺,“焦炉气甲烷化制备天然气”工艺和“焦炉气联合净化分离制备天然气”工艺.介绍了目前国内焦炉气制天然气技术拥有单位或个人专利申请情况,指出焦炉气制天然气项目的实施对焦化行业节能减排及发展循环经济等具有重要意义.

  7. Correlation between porous structure and fracture stress for metallurgical coke

    Energy Technology Data Exchange (ETDEWEB)

    Gardien, J.F.; Lemaire, E.; Dubs, A.; Osmont, P.; Laurent, J.P.; Steiler, J.M. (Institut de Recherches de la Siderurgie Francaise, Maizieres-les-Metz (France))

    1994-05-26

    Various samples of coke have been characterized by diametral compression and the geometry of the porous network has been analysed in terms of fractal structure. It is found that the coke studied exhibits a fractal behaviour on at least two decades. Diametral compression test leads to two different ways of breaking; brittle fracture, and in some cases complex fracture. As expected, the fracture stress is not linked with the fractal dimension in case of brittle fracture, but with the mean size of the largest pores. In case of complex loading conditions, the fracture strength is linked with the fractal dimension. The models of Cook and of Anderson, which integrate fractal description of porous materials in Griffith's theory, do not seem to be valid concerning coke material. The present approach of characterising the porous structure of coke by the fractal dimension seems adapted to explain coke strength, especially under complex stress conditions, but should be extended to an increased number of coke type samples.

  8. Fissure formation in coke. 1: The mechanism of fissuring

    Energy Technology Data Exchange (ETDEWEB)

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

    2010-07-15

    Pilot scale coke oven experiments, in which carbonisation has been arrested after 2 and 4 h, have been used to identify key aspects of the initial formation and propagation of fissuring in coke. The experiments show that the primary fissure network is formed within the first few hours of coking and the fissures propagate towards the centre of the oven as coking progresses. They also show that some of the initially formed fissures stop propagating, thus increasing the effective fissure spacing as coking continues. A model for the propagation of regular crack arrays has been used to identify the cause of the initial formation of the fissure network, evaluate the fissure spacing and explain the fissure coarsening effect. The coarsening is shown to be due to an instability, in the form of every second fissure stopping. The formation of lateral fissures is shown to be due to tensile stress formation near the tips of stopped fissures and also to increased shrinkage due to a maximum in the coke contraction coefficient at around 700{sup o}C. 45 refs., 11 figs., 1 tab.

  9. Damage Diagnosis for High Temperature Coke-oven Chamber Walls

    Science.gov (United States)

    Sugiura, Masato; Sakaida, Michitaka; Fujikake, Yohichi; Irie, Keisuke

    Metallurgical coke is needed as reducing reagent and energy source in blast furnaces. Most of coke ovens in Japan have been working over 30 years and have become gradually decrepit. A coke oven consists of many coking chambers, and each chamber is 6 m high, 16 m long and 0.4m wide. Uneven damage at the chamber-wall surface such as brick erosion and carbon deposition disturbs production because the coke is pushed horizontally when discharged from the chamber. To diagnose the chamber wall which is constantly sustained at a high temperature, we have developed a water-cooling heat-resistance probe. Line scan cameras mounted in the probe obtain thermal images of the entire chamber-wall surfaces with high resolution. In addition, to measure topographical information of the wall, a laser light-section method combined with line-scan-camera imaging has been considered. It is emphasized that the diagnosis probe works under enormously severe conditions, such as at a temperature of over 1000°C and inside a width of only 0.4m. Clarifying the appearance of chamber-wall damages in operating aged coke ovens, we proposed the index relating unevenness of a chamber-wall surface to pushing load. The index is utilized for the guidance enabling effective repairs of damaged oven walls.

  10. 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.

  11. Clean cars

    Energy Technology Data Exchange (ETDEWEB)

    Piffaretti, M.

    2008-07-01

    This well-illustrated presentation made at the Swiss 2008 research conference on traffic by the Protoscar company takes a look at research, design, engineering and communication topics in the area of 'clean cars'. The present situation with electrically driven and hybrid-drive cars is reviewed and the chances and problems of the present-day vehicles are examined. New developments and a number of vehicles that should be on the market in the period from 2012 to 2015 are presented. Also, 'clean' specialist vehicles such as trucks and buses are reviewed. Battery systems and associated problems and new developments are looked at. The promotion scheme in Mendrisio, Switzerland is reviewed. Bottom-up and top-down approaches are discussed and future market developments are looked at, as are promotional activities in various countries.

  12. 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.

  13. Effect of paste humidity on kinetics of carbothermal reduction of extruded barite and coke mixture

    Science.gov (United States)

    Salem, A.; Jamshidi, S.

    2012-08-01

    The effect of the moisture content of barite-coke paste on the kinetics of carbothermal reduction was investigated to understand the role of extrusion technique on this type of solid-gas reaction. The pastes were formulated using the typical natural barite and coke powders normally used in the industrial scale. 0.65 wt.% carboxyl methyl cellulose and different amounts of distilled water, ranging 24.3-34.4% were added to the mixed powders. The obtained pastes were then shaped by a laboratory extruder. The extrusion process was assessed by determining the total porosity of dry samples. The samples in the form of disc were isothermally heated at different temperatures in the range of 800-950 °C and the conversion of barite into barium sulfide was measured by the iodometry. The reduction data were analyzed by a modified kinetic model and the frequency factor and activation energy were calculated to evaluate the reduction mechanism. It was found that the moisture content of the paste significantly affects the active site density due to increasing contact surface area between coke and barite particles.

  14. The effect of treatment stages on the coking wastewater hazardous compounds and their toxicity.

    Science.gov (United States)

    Wei, Xiao-xue; Zhang, Zi-yang; Fan, Qing-lan; Yuan, Xiao-ying; Guo, Dong-sheng

    2012-11-15

    This study investigated the change of hazardous materials in coking wastewater at different treatment stages (anaerobic, anaerobic/aerobic, anaerobic/aerobic/photo degradation, anaerobic/aerobic/ozone oxidation treatment) and the effects of them on the development of maize embryos and the activity of amylase and protease in maize seeds. Moreover the interaction of refractory organic matters in the wastewater at different treatment stages with amylase and protease also were determined in vitro. The results show that the biodegradable and the refractory organic compounds in the wastewater both can affect maize embryo development (germination inhibition rate is 19.3% for biodegradable organic compounds). As the treatment stage preceding, the inhibition effect of coking wastewater on the development of the maize embryo (for germination inhibition rates change from 49.3% to 24.6%) and on enzymatic activity (inhibition rates change from 63.9% to 22.4% for amylase) decreases gradually, but the photo-degradation treatment to anaerobic/aerobic effluent can increase its toxicity. The changes in the ability of the refractory organic compounds to bind with enzyme proteins, combined with the analysis of the organic components by GC/MS, show that in the process of coking wastewater treatment no new toxic chemicals were produced. PMID:23022415

  15. Ionic Liquid Catalyst Used in Deep Desulfuration of the Coking Benzene for Producing Sulfurless Benzene

    Institute of Scientific and Technical Information of China (English)

    ZHOU Xia-Ping; WANG Yan-Liang; MENG Fan-Wei; FAN Xing-Ming; QIN Song-Bo

    2008-01-01

    For the widening need of benzene used in organic synthesis, ionic liquid catalyst was prepared to study the process of deep desulfuration in the coking benzene. The result shows that the effect of de-thiophene by the ionic liquid catalyst (N-methyl imidazolium hydrogen sulfate [Hmim][HSO4]) is related to its acid function value.Hammett indicator was used to determine the acid function value H0 of the ionic liquid. It can be concluded that while the acid function value is in the range from -4 to -12, the ionic liquid catalyst can make the concentration certain acid quantity and strength, the ionic liquid catalyst helps to form alkyl thiophene through Friedel-Crafts reaction, which differs from the character of benzene and it is absolutely necessary for the separation and refinement of benzene. But overabundant quantity and higher acid value of [Hmim][HSO4] are more suitable for the side copolymerization of benzene, thiophene and alkene, thereby affecting repeated use of the ionic liquid catalyst([Hmim][HSO4]). In our research, thiophene derivant produced by desulfurization in the coking benzene was used as the polymer to provide the passing channel of the charges. The ionic liquid composition in poor performance after repeated use was made to prepare conductive material (resisting to static electricity) as an "electron-receiving" and "electron-giving" doping agent. The result shows that thiophene derivant after desulfuration in the coking benzene can be used to prepare doping conductive materials.

  16. Coupling thermogravimetric and acoustic emission measurements: its application to study the inhibition of catalytic coke deposition

    Energy Technology Data Exchange (ETDEWEB)

    Ropital, Francois; Dascotte, Philippe; Marchand, Pierre [Institut Francais du Petrole, 1 Avenue Bois Preau, 92952 Rueil-Malmaison (France); Faure, Thierry; Lenain, Jean-Claude; Proust, Alain [Euro Physical Acoustics, 27 Rue Magellan, 94373 Sucy-en-Brie Cedex (France)

    2004-07-01

    In order to improve the knowledge on the high temperature behaviour of metallic materials, the coupling of several in situ physical analysis methods is a promising way. For this purpose a thermogravimetric balance has been equipped with a specific acoustic emission device in order to continuously measure the mass variation of the corrosion sample and the acoustic emission transient under experimental conditions of temperature and gas phase compositions that are representative of the industrial environments. The catalytic coke deposition condition that is a major problem for the refinery and petrochemical industries, has been studied with such a device. The carbon deposition on reactor walls can induce localised disruption in the process such as heat-transfer reduction and pressure drops. To prevent these perturbations, proper selections of the metallurgical or internal coating compositions of the equipment, or the injection of accurate amount of inhibitors have to be decided. The feasibility of the coupling at high temperature of thermogravimetric and acoustic emission has been demonstrated. This new technique has been applied to study the inhibition of the catalytic coke deposition on pure iron by sulphur additives in the temperature range of 650 deg. C and under different mixed atmospheres of hydrocarbon and hydrogen contents. Good correlation has been obtained between the coking rates measured by thermogravimetric measurements and the intensities of the acoustic emission parameters. (authors)

  17. Joint Implementation Analysis: A Case Study of the Japan-China Coke Dry Quenching (CDQ) Project

    Institute of Scientific and Technical Information of China (English)

    2000-01-01

    One of the key issues for "Joint Implementation" is how to define a plausible baseline, a necessary benchmark for calculating net Greenhouse Gases (GHGs) emission reductions through a comparative approach. Based on a thorough case study of the China-Japan Coke Dry Quenching (CDQ) project, the first approved pilot project in China under the "Activities Implemented Jointly" (AIJ) framework, the paper not only describes in detail the complete procedure of baseline definition of the case project, but also discusses its approach to baseline determination. Furthermore, cost-benefit analysis of GHGs mitigation is conducted according to the baseline. This empirical case study, based on real AIJ project data, will be beneficial for the development of future projects under Kyoto mechanisms such as "Clean Development Mechanism" and "Joint Implementation".

  18. Refinaria do Nordeste: petroleum coke handling system; Refinaria do Nordeste: desafios do sistema de movimentacao de coque verde de petroleo

    Energy Technology Data Exchange (ETDEWEB)

    Medeiros, Luiz G. de; Cabral, Jose Mauro B. [PETROBRAS S.A., Ipojuca, PE (Brazil). Refinaria do Nordeste (RNEST); Lucredi, Hedewandro A. [PETROBRAS S.A., Paulinia, SP (Brazil). Refinaria de Paulinia (REPLAN); Barros, Francisco Carlos da C. [PETROBRAS S.A., Rio de Janeiro, RJ (Brazil). Centro de Pesquisas (CENPES)

    2008-07-01

    The Delayed Coking Units - DCU - are adequate to the scheme for processing heavy oils where the market of fuel oil or asphalt is low or not profitable. The DCU's are conversion units that produce, in addition to the gas and liquid distilled products, the petcoke. The petcoke, depending on the characteristics, is used in various applications like as in the aluminum, iron, thermoelectric and cement industries. The petcoke is solid and its logistics is quite different from most of the products handled by PETROBRAS; therefore, this product has been a constant challenge in relation to the market requirements. Due to the importance of the DCU at Refinaria do Nordeste, and the petcoke production capacity, the coke handling system was projected in order to ensure the refinery operational continuity. The project permits the expedition and loading of 10,000 tons of petcoke within a period of 12 hours of work for cargo vessel. In the development of the processing project of Refinaria do Nordeste efforts were made to optimize the Delayed Coking Unit for the production of distilled products and the quality of the coke. The DCU operating conditions were projected so as to produce petcoke with quality adequate to the iron and aluminum industry. (author)

  19. Gas-Liquid Supersonic Cleaning and Cleaning Verification Spray System

    Science.gov (United States)

    Parrish, Lewis M.

    2009-01-01

    NASA Kennedy Space Center (KSC) recently entered into a nonexclusive license agreement with Applied Cryogenic Solutions (ACS), Inc. (Galveston, TX) to commercialize its Gas-Liquid Supersonic Cleaning and Cleaning Verification Spray System technology. This technology, developed by KSC, is a critical component of processes being developed and commercialized by ACS to replace current mechanical and chemical cleaning and descaling methods used by numerous industries. Pilot trials on heat exchanger tubing components have shown that the ACS technology provides for: Superior cleaning in a much shorter period of time. Lower energy and labor requirements for cleaning and de-scaling uper.ninih. Significant reductions in waste volumes by not using water, acidic or basic solutions, organic solvents, or nonvolatile solid abrasives as components in the cleaning process. Improved energy efficiency in post-cleaning heat exchanger operations. The ACS process consists of a spray head containing supersonic converging/diverging nozzles, a source of liquid gas; a novel, proprietary pumping system that permits pumping liquid nitrogen, liquid air, or supercritical carbon dioxide to pressures in the range of 20,000 to 60,000 psi; and various hoses, fittings, valves, and gauges. The size and number of nozzles can be varied so the system can be built in configurations ranging from small hand-held spray heads to large multinozzle cleaners. The system also can be used to verify if a part has been adequately cleaned.

  20. 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 ...

  1. Mechanism for sludge acidification in aerobic treatment of coking wastewater

    International Nuclear Information System (INIS)

    This work was undertaken to investigate the cause of sludge acidification that led to disruption of the activated sludge process treating coking wastewater from a steel-making plant in Taiwan. An activated sludge reactor (ASR) with a working volume of 80 L was used as a model system to simulate the behavior of the real wastewater treatment process. Parameters that may cause acidification or inactivation of the sludge (NH3, SCN-, S2O32- and CN-) were studied individually to examine for their effects on the performance of the ASR. The results show that high loading of NH3, SCN- and CN- did not lead to pH decrease, while the ASR attained 85% COD removal and nearly 100% SCN degradation. In contrast, when the wastewater was supplemented with ca. 1000 mg/L of S2O32-, the pH dropped to nearly 4.0 in 2 days and the COD and SCN removal yields were significantly lower (at 50 and 0-20%, respectively). Thus, overloading of S2O32- was apparently a key factor causing sludge acidification. The results suggest that to ensure a normal functioning of the activated sludge, the influent S2O32- concentration should be closely monitored and that the pH control of the ASR is indispensable when the S2O32- loading is in excess

  2. 焦炉加热废气中 CO 含量的控制%Control of CO content in waste gas by coke oven heating

    Institute of Scientific and Technical Information of China (English)

    马志; 王进先

    2014-01-01

    简述了CO的危害及焦炉加热对废气中CO含量的影响因素,通过控制空气过剩系数、加强新建焦炉砌筑管理、高炉煤气加热时使用交换旋塞、换向期间增设空气清扫装置、安装在线仪表检测废气成分、加强焦炉日常热修维护等技术措施可有效降低焦炉废气中 CO的含量。%The harm of CO as well as the factors effected CO content in waste gas by coke oven heating is summarized .CO content in coke oven waste gas can be reduced efficiently by technical measures such as controlling excess air factors ,bettering bricklaying management of newly-built coke oven,using reversing cocks during BFG heating ,adding air cleaning device during reversing ,instal-ling on-line instruments to detect the content of the waste gas ,and emphasizing routine hot mainte-nance for coke oven .

  3. Study on the adsorption characteristics of modified semi-coke used for treating biologically treated effluent from coking wastewater%改性兰炭对焦化废水生化出水的吸附特性

    Institute of Scientific and Technical Information of China (English)

    王丽娜; 刘尚超; 张垒; 付本全

    2012-01-01

    Semi-coke that has been modified with steam at high temperature is used for the static adsorption of TOC in biochemically treated effluent from coking wastewater. The effects of influencing factors, such as adsorption time, pH,adsorbent dosage,particle size,etc.,on the treatment efficiency are investigated. The results show that after adding 20 g/L 1 -2 mm of modified semi-coke to wastewater whose pH is 4, at room temperature and adsorption time 30 min,the TOC removing rate of biochemically treated effluent from the coking wastewater is more than 60%. The concentration and variety of the organisms in samples after the adsorption process have decreased greatly.%利用水蒸气高温改性后的兰炭静态吸附焦化废水生化出水中的TOC,考察了吸附时间、pH、吸附剂用量、粒径等因素对处理效果的影响.结果表明,向废水(pH=4)中投加20 g/L改性兰炭(粒径1~2 mm),室温下吸附30 min后,对焦化废水生化出水的TOC去除率在60%以上.吸附后水样中的有机物浓度和种类都大幅下降.

  4. Electrochemical treatment of COD in biologically pretreated coking wastewater using Ti/RuO2-IrO2 electrodes combined with modified coke

    Institute of Scientific and Technical Information of China (English)

    HE Xu-wen; LIU Li-yuan; GONG Jing-wen; WANG Jian-bing; QIN Qiang; WANG Hao

    2011-01-01

    The electrochemical treatment of COD contained in biologically pretreated coking wastewater treated by a three-dimensional electrode system with modified coke as the particle electrode was investigated.And the electrochemical perfomance of the coke modified with various active components was studied.The results show that the coke modified with Fe(NO3)2 has the lowest energy consumption and higher COD removal rate under the same condition,and the modified coke has better surface characteristics for the purpose of this study.In addition,the kinetic constant was also calculated.The study shows that the three-dimensional electrode system with Fe(NO3)2-modified coke can give a satisfactory solution in biologically pretreated coking wastewater.

  5. NON-SPECIFIC METHODS FOR DETECTING RESIDUES OF CLEANING AGENTS DURING CLEANING VALIDATION

    OpenAIRE

    DRAGAN M. MILENOVIĆ; DRAGAN S. PEŠIĆ; SNEŽANA S. MITIĆ

    2011-01-01

    Cleaning validation procedures are carried out in order to assure that residues of cleaning agents are within acceptable limits after the cleaning process. Cleaning agents often consist of a mixture of various surfactants which are in a highly diluted state after the water rinsing procedure has been completed. This makes it difficult to find appropriate analytical methods that are sensitive enough to detect the cleaning agents. In addition, it is advantageous for the analytical methods to be ...

  6. Hydrocarbonization process evaluation report. Volume II. Evaluation of process feasibility. [49 refs

    Energy Technology Data Exchange (ETDEWEB)

    Holmes, J.M.; Dyslin, D.A.; Edwards, M.S.; Joy, D.S.; Peterson, G.R.

    1977-07-01

    Volume II of a two-volume study concerning the preliminary design and economic evaluation of a Hydrocarbonization Facility includes: (1) a review of the current status of the major processing units, (2) an assessment of operating problems, (3) considerations of possible process alternatives, (4) an evaluation of the overall process feasibility, and (5) recommendations for future process development. Results of the study emphasize the need for testing the evaluated process, which is based on the Clean Coke Process, in a continuous pilot plant using a wide variety of highly caking bituminous coals as feed material. A program suggested for the pilot plant would encompass: (1) development of improved methods for the prevention of agglomeration of highly caking coals during hydrocarbonization, (2) optimization of the yields of coal liquids, (3) investigation of a single-stage high-temperature hydrocarbonizer optimized for char production, and (4) optimization of beneficiation ratios employed during coal preparation.

  7. Investigations concerning the mechanism of action of brown-coal coke particles in aerobic biological waste water treatment

    International Nuclear Information System (INIS)

    At the start of this work experience with the use of brown coal coke in the activated sludge process was lacking entirely. It therefore was necessary to carry through preliminary experiments in order to practically test the effect of Grown-coal coke. In two technical-scale experiments and a pilot test, very good results were obtained with the application of brown-coal coke to activated sludge. These, and previously published results, permitted to evolve moodel concepts of the mechanism of action of coal, especially brown coal coke, in activated sludge. According to these concepts the coal particles act as buffers and a temporary adsorbent of oxygen and waste water constituents. This in turn stimulates the colonization of the surface with microorganisms. In order to corroborate these model concepts, the - adsorption and desorption of solved oxygen to coal in a watery medium and - the effect of coal over a longer period of time were investigated. The results in essence confirm the model concepts. (UWa)

  8. Coking Wastewater Treatment by Coke Powder Activation%焦粉活化处理焦化废水

    Institute of Scientific and Technical Information of China (English)

    彭兴华; 张远行

    2012-01-01

    In our report, activated coke and coking wastewater treatment were performed by changing the chemical reagent type, concentration and time, and the removal rates of activated coke on volatile phenol, COD substances, ammonia and non-ferrous material in coking wastewater were analyzed. The results indicated that the effects of steam modified coke powder were superior to that of chemical reagent modified coke powder; the volatile phenol removal rate, COD removal rate, ammonia-nitrogen removal rate and chroma removal rate of which was 98.67% , 83.05% , 37.52% , 94. 71% , respectively; the ammonia-nitrogen removal rate of coke powder treated with HNO3(5 mol · L-1) attained 49.33%.%通过改变化学试剂种类、浓度和时间等3个因素来活化焦粉并处理焦化废水的实验,研究了活化焦粉对焦化废水中的挥发酚、COD物质、氨氮和有色物的去除率.结果表明:水蒸气改性焦粉的处理效果优于化学试剂改性焦粉的处理效果.水蒸气改性后的焦粉,其处理废水中挥发酚的去除率可达98.67%,COD去除率可达83.05%,氨氮去除率可达37.52%,色度去除率可达94.71%.采用5mol·L-1的HNO3活化焦粉,氨氮去除率效果较好,可达49.33%.

  9. 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: (i) making coke of such quality as to be suitable for use in hard-driving, large blast furnaces; (ii) providing proof that such process is continuous and environmentally closed to prevent emissions; (iii) 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 (iv) 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: Consolidation of the project team-players; Recruiting Koppers Industries as an additional stakeholder; Developing a closed system for the production of binder pitch from tar in the Calderon coking process as the incentive for Koppers to join the team; Gathering appropriate equipment for conducting a set of experiments at bench scale to simulate tar quality produced from the Calderon coking process for the production of binder pitch; and Further progress made in the design of the commercial coking reactor

  10. Pretreatment of coking wastewater using anaerobic sequencing batch reactor (ASBR)

    Institute of Scientific and Technical Information of China (English)

    LI Bing; SUN Ying-lan; LI Yu-ying

    2005-01-01

    A laboratory-scale anaerobic sequencing batch reactor (ASBR) was used to pretreat coking wastewater. Inoculated anaerobic granular biomass was acclimated for 225 d to the coking wastewater, and then the biochemical methane potential (BMP)of the coking wastewater in the acclimated granular biomass was measured. At the same time, some fundamental technological factors, such as the filling time and the reacting time ratio (tf/tr), the mixing intensity and the intermittent mixing mode, that affect anaerobic pretreatment of coking wastewater with ASBR, were evaluated through orthogonal tests. The COD removal efficiency reached 38%~50% in the stable operation period with the organic loading rate of 0.37~0.54 kg COD/(m3.d) at the optimum conditions of tf/tr, the mixing intensity and the intermittent mixing mode. In addition, the biodegradability of coking wastewater distinctly increased after the pretreatment using ASBR. At the end of the experiment, the microorganism forms on the granulated sludge in the ASBR were observed using SEM (scanning electron microscope) and fluoroscope. The results showed that the dominant microorganism on the granular sludge was Methanosaeta instead of Methanosarcina dominated on the inoculated sludge.

  11. Industrial Experiment on Coke Spraying With ZBS Additive in Blast Furnace

    Institute of Scientific and Technical Information of China (English)

    ZHU Zi-zong; ZHANG Zhu-ming; TANG Qi-yong; YANG Xue-feng; ZHANG Kun-hua; ZHAO Xian-sheng

    2006-01-01

    In order to improve the thermal properties of coke, an industrial experiment on the coke spraying with ZBS additive solution was carried out at coking plant and No.6 blast furnace (2 000 m3) of Kunming Iron and Steel Co Ltd. The coke reaction index (CRI) of the coke spraying with ZBS additive solution decreases by 10.56%, and the coke strength after reaction (CSR) increases by 7.80% in comparison with those of the un-sprayed coke. During the experiment, the average iron output increases by 66.69 t/d, and the coke rate is reduced by 5.21 kg per ton iron, while the fluctuation of furnace temperture is small, and sulphur content in hot metal and 100% of hot metal are acceptable.

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

    OpenAIRE

    Jesús Manuel Gutierrez Bernal; William Fernando Mora Pulido; Luís Ignacio Rodríguez Varela; Javier Ramírez; José de Jesús Díaz Velásquez

    2011-01-01

    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 c...

  13. 超声波清洗牛肚的工艺优化%Process Optimization for the Ultrasonic Cleaning of Bovine Tripe

    Institute of Scientific and Technical Information of China (English)

    蔡丹; 张大力; 盛悦; 宫田娇; 原秀玲; 文超婷; 刘景圣

    2015-01-01

    The process optimization for the ultrasonic cleaning of bovine tripe was carried out by investigating the influence of ultrasonic power, cleaning time and temperature on the cleanliness and total bacterial count (TBC) of bovine tripe. Results showed that the cleanliness and TBC of bovine tripe could be improved effectively by the treatment with an ultrasonic power of 350 W for 30 min at 25℃ to 0.93± 0.26 and (5.04± 1.53) (lg(CFU/g)), respectively.%以牛肚为主要原料,研究不同超声波功率、清洗时间和清洗温度对牛肚洁净度和菌落总数的影响,优化超声波清洗牛肚的工艺条件。结果表明:在超声波功率为350 W,超声波清洗时间为30 min,清洗温度为25℃的工艺条件下,牛肚的洁净度和菌落总数分别为0.93±0.26和(5.04±1.53)(lg(CFU/g)),达到最佳清洗效果。

  14. Self-cleaning Metal Organic Framework (MOF) based ultra filtration membranes--a solution to bio-fouling in membrane separation processes.

    Science.gov (United States)

    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 carboxylic and amine functional groups. The innovative surface chemistry helps to reduce the contact angle of the novel membrane by at least a 48% and increase the pure water flux by 39.4% compared to the control membrane. The flux drop for the novel membrane is also lower (16.3% of the initial flux) than the control membrane (55.3% of the initial flux) during the long term experiments with protein solution. Moreover, the novel membrane continues to exhibit inhibition to microbes even after 1320 min of protein filtration. Synthesis of self-cleaning ultrafiltration membrane with long lasting properties opens up a viable solution for bio-fouling in ultrafiltration application for wastewater purification. PMID:25296745

  15. Self-cleaning Metal Organic Framework (MOF) based ultra filtration membranes - A solution to bio-fouling in membrane separation processes

    Science.gov (United States)

    Prince, J. A.; Bhuvana, S.; Anbharasi, V.; Ayyanar, N.; Boodhoo, K. V. K.; Singh, G.

    2014-10-01

    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 carboxylic and amine functional groups. The innovative surface chemistry helps to reduce the contact angle of the novel membrane by at least a 48% and increase the pure water flux by 39.4% compared to the control membrane. The flux drop for the novel membrane is also lower (16.3% of the initial flux) than the control membrane (55.3% of the initial flux) during the long term experiments with protein solution. Moreover, the novel membrane continues to exhibit inhibition to microbes even after 1320 min of protein filtration. Synthesis of self-cleaning ultrafiltration membrane with long lasting properties opens up a viable solution for bio-fouling in ultrafiltration application for wastewater purification.

  16. Self-cleaning Metal Organic Framework (MOF) based ultra filtration membranes--a solution to bio-fouling in membrane separation processes.

    Science.gov (United States)

    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 carboxylic and amine functional groups. The innovative surface chemistry helps to reduce the contact angle of the novel membrane by at least a 48% and increase the pure water flux by 39.4% compared to the control membrane. The flux drop for the novel membrane is also lower (16.3% of the initial flux) than the control membrane (55.3% of the initial flux) during the long term experiments with protein solution. Moreover, the novel membrane continues to exhibit inhibition to microbes even after 1320 min of protein filtration. Synthesis of self-cleaning ultrafiltration membrane with long lasting properties opens up a viable solution for bio-fouling in ultrafiltration application for wastewater purification.

  17. A system of metadata to control the process of query, aggregating, cleaning and analysing large datasets of primary care data

    Directory of Open Access Journals (Sweden)

    Jeremy VanVlymen

    2005-12-01

    Conclusions The PCDQ metadata system provides an auditable method of data processing. It is a method that should improve the reliability, validity and efficiency of processing routinely collected clinical data. This paper sets out to demystify our data processing method and makes the PCDQ metadata system available to clinicians and data processors who might wish to adopt it.

  18. Textural changes in metallurgical coke prepared with polyethylene

    Institute of Scientific and Technical Information of China (English)

    Stanislav S.Gornostayev; Jyrki J.Heino; Tommi M.T.Kokkonen; Hannu T.Makkonen; Satu M.M.Huttunen; Timo M.J.Fabritius

    2014-01-01

    The effect of high-density polyethylene (HDPE) on the textural features of experimental coke was investigated using polar-ized-light optical microscopy and wavelet-based image analysis. Metallurgical coke samples were prepared in a laboratory-scale furnace with 2.5%, 5.0%, 7.5%, 10.0%, and 12.5%HDPE by mass, and one sample was prepared by 100%coal. The amounts and distribution of textures (isotropic, mosaic and banded) and pores were obtained. The calculations reveal that the addition of HDPE results in a decrease of mosaic texture and an increase of isotropic texture. Ethylene formed from the decomposition of HDPE is considered as a probable reason for the texture modifications. The approach used in this study can be applied to indirect evaluation for the reactivity and strength of coke.

  19. Interactions between coking coals and plastics during co-pyrolysis

    Energy Technology Data Exchange (ETDEWEB)

    Richard Sakurovs [CSIRO, North Ryde, NSW (Australia). Division of Energy Technology

    2003-10-01

    Blends of three Australian coking coals and polypropylene, polystyrene, polyacrylonitrile and polyphenylene sulfide were prepared and the extent to which the blends fused on heating was monitored using proton magnetic resonance thermal analysis in order to identify interactions between them that could affect their fluidity. Different plastics had different effects. Polystyrene strongly reduced the fluidity of all of the coals, confirming previous findings. Polypropylene did not affect the fluidity of the two coking coals of lower rank. Polyphenylene sulfide reduced the fluidity of the coals at temperatures near the solidification temperature of the coals, and polyacrylonitrile appeared to increase the fluidity of the coals at temperatures near the softening temperature of the coals. The very different effects different plastics have on coal fluidity show that the interaction between plastics and coals must be carefully examined before plastics are added to coking coal blends. 28 refs., 6 figs., 1 tab.

  20. State of the direct reduction and reduction smelting processes

    Directory of Open Access Journals (Sweden)

    Markotić A.

    2002-01-01

    Full Text Available For quite a long time efforts have been made to develop processes for producing iron i.e. steel without employing conventional procedures - from ore, coke, blast furnace, iron, electric arc furnace, converter to steel. The insufficient availability and the high price of the coking coals have forced many countries to research and adopt the non-coke-consuming reduction and metal manufacturing processes (non-coke metallurgy, direct reduction, direct processes. This paper represents a survey of the most relevant processes from this domain by the end of 2000, which display a constant increase in the modern process metallurgy.

  1. Precision Cleaning - Path to Premier

    Science.gov (United States)

    Mackler, Scott E.

    2008-01-01

    ITT Space Systems Division s new Precision Cleaning facility provides critical cleaning and packaging of aerospace flight hardware and optical payloads to meet customer performance requirements. The Precision Cleaning Path to Premier Project was a 2007 capital project and is a key element in the approved Premier Resource Management - Integrated Supply Chain Footprint Optimization Project. Formerly precision cleaning was located offsite in a leased building. A new facility equipped with modern precision cleaning equipment including advanced process analytical technology and improved capabilities was designed and built after outsourcing solutions were investigated and found lacking in ability to meet quality specifications and schedule needs. SSD cleans parts that can range in size from a single threaded fastener all the way up to large composite structures. Materials that can be processed include optics, composites, metals and various high performance coatings. We are required to provide verification to our customers that we have met their particulate and molecular cleanliness requirements and we have that analytical capability in this new facility. The new facility footprint is approximately half the size of the former leased operation and provides double the amount of throughput. Process improvements and new cleaning equipment are projected to increase 1st pass yield from 78% to 98% avoiding $300K+/yr in rework costs. Cost avoidance of $350K/yr will result from elimination of rent, IT services, transportation, and decreased utility costs. Savings due to reduced staff expected to net $4-500K/yr.

  2. 40 CFR 63.302 - Standards for by-product coke oven batteries.

    Science.gov (United States)

    2010-07-01

    ... batteries. 63.302 Section 63.302 Protection of Environment ENVIRONMENTAL PROTECTION AGENCY (CONTINUED) AIR... National Emission Standards for Coke Oven Batteries § 63.302 Standards for by-product coke oven batteries... oven emissions from each affected existing by-product coke oven battery that exceed any of...

  3. Renewable synthesis-gas-production. Do hydrocarbons in the reactant flow of the reverse water-gas shift reaction cause coke formation?

    Energy Technology Data Exchange (ETDEWEB)

    Wolf, A.; Kern, C.; Jess, A. [Bayreuth Univ. (Germany). Dept. of Chemical Engineering

    2013-11-01

    In a two-step synthetic fuel production process based on carbon dioxide and renewable hydrogen, the best possible selectivity towards liquid hydrocarbons (Hc) shall be implemented. The process consists of a combination of the Reverse Water-Gas Shift reaction and the Fischer-Tropsch synthesis. To achieve this goal, gaseous short-chained Hc from the FTS reactor are recycled in the RWGS unit. In this paper, challenges coming up with the implementation of a recycle loop are discussed. First of all, it has to be examined whether Hc are converted under conditions present in the RWGS reactor. The coking caused by the recycle of Hc is regarded, including thermal coking in the heating zone of the reactor and catalytic coking in the catalyst bed. Coking of course is unwanted, as it deactivates the catalyst. The scope of this work is to find out to which extent and under which conditions gaseous Hc can be recycled. Therefore, experiments were carried out in both, a quartz glass reactor using a commercial Ni-catalyst at ambient pressure and in a pressurized steel reactor (without catalyst) to examine coking during the thermal decomposition of Hc. The catalytic experiments at atmospheric pressure showed that a recycle of CH{sub 4} did not cause coking up to a ratio of CH{sub 4}/CO{sub 2} below one. For these conditions, long term stability was proved. The reaction rates of the CH{sub 4} conversion were below those of the RWGS reaction. However, replacing CH{sub 4} by C{sub 3}H{sub 8} leads to thermal and catalytic coking. Catalytic coking hits the maximum level at about 700 C and decreases for higher temperatures and, thus is not regarded as a problem for the RWGS reactor. In contrast to that, thermal coking raises with higher temperatures, but it can be supressed efficiently with additional injection of H{sub 2}O, which of course shifts the equilibrium towards the undesired reactant side. (orig.)

  4. [Characterization of PAHs in fly ashes from coke production].

    Science.gov (United States)

    Mu, Ling; Peng, Lin; Liu, Xiao-Feng; Bai, Hui-Ling; Zhang, Jian-Qiang

    2013-03-01

    In order to investigate the characteristics of polycyclic aromatic hydrocarbons (PAHs) in ashes from coking, PAHs in ashes from three coke production plants were analyzed with GC-MS, and the distribution characteristics of PAHs and potential toxicity risk were discussed. The sum of 16 EPA prior PAHs varied from 8.17 x 10(2) to 5.17 x 10(3) microg x g(-1). PAH contents from the coke oven (stamp charging) with the height of 3.2 m were two times higher than those from the one (top charging) with the height of 6.0 m, and PAHs in ashes from coal charging were significantly higher than those from coke pushing in the same plant. Four-ring and five-ring PAHs were the dominant species in ashes from coking and the sum of them accounted for more than 80.00% of total PAHs. Chrysene (Chr), benzo [a] anthracene (BaA) and benzo [b] fluoranthene (BbF) were abundant in all ash samples. The content of total BaP-based toxic equivalency (BaPeq) ranged from 1.64 x 10(2) to 9.57 x 10(2) microg x g(-1). From the carcinogenic point of view, besides benzo [a] pyrene (BaP), dibenz [a,h] anthracene (DbA) contributed most to the overall toxicity of PAHs, followed by BaA and BbF. BaPeq concentration from coal charging was 5.21-fold higher than that from coke pushing, indicating that different reuse ways should be considered based on their specific toxicity profiles of PAHs. PMID:23745428

  5. Efficient methods of nanoimprint stamp cleaning based on imprint self-cleaning effect

    International Nuclear Information System (INIS)

    Nanoimprint lithography (NIL) is a nonconventional lithographic technique that promises low-cost, high-throughput patterning of structures with sub-10 nm resolution. Contamination of nanoimprint stamps is one of the key obstacles to industrialize the NIL technology. Here, we report two efficient approaches for removal of typical contamination of particles and residual resist from stamps: thermal and ultraviolet (UV) imprinting cleaning-both based on the self-cleaning effect of imprinting process. The contaminated stamps were imprinted onto polymer substrates and after demolding, they were treated with an organic solvent. The images of the stamp before and after the cleaning processes show that the two cleaning approaches can effectively remove contamination from stamps without destroying the stamp structures. The contact angles of the stamp before and after the cleaning processes indicate that the cleaning methods do not significantly degrade the anti-sticking layer. The cleaning processes reported in this work could also be used for substrate cleaning.

  6. Optimization of the coke-oven activated sludge plants

    Energy Technology Data Exchange (ETDEWEB)

    Raizer Neto, Ernesto [Santa Catarina Univ., Florianopolis, SC (Brazil); Colin, Francois [Institut de Recherches Hydrologiques, 54 - Nancy (France); Prost, Christian [Laboratoire de Sciences de Genie Chimique, Nancy (France)

    1993-12-31

    In the coke-oven activated sludge plants one of the greatest problems of malfunction is due to inffluent variability. The composition and, or, concentration variations of the inffluent substrate, which can cause an unstable system, are function of the pollutant load. Nevertheless, the knowledge of the kinetic biodegradation of the coke-oven effluent represents the limiting factor to develop an effective biological treatment. This work describes a computational model of the biological treatment which was elaborated and validated from continuous pilot scale experiments and calibrated by comparing its predictions to the pilot experiment`s results. 12 refs., 9 figs., 3 tabs.

  7. Characterisation of coking activity during supercritical hydrocarbon pyrolysis

    OpenAIRE

    Gascoin, Nicolas; Gillard, Philippe; Bouchez, Marc

    2008-01-01

    cited By (since 1996) 5 International audience 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 an...

  8. Methods for measuring moisture content in the coal and coke

    International Nuclear Information System (INIS)

    As a result of modern mining methods and the increase of fine coal recovery for economic reasons, there has been growing interest in measuring and controlling the moisture content of the coal and coke. In recent decades moisture determination of the coal and coke has been extensively investigated and applied worldwide. The methods for measuring moisture include nuclear and non-nuclear techniques. This paper introduces the basic principle and principal specification of various techniques for moisture determination and reviews advantage and disadvantage for various methods and also put forward the tendency at present

  9. 利用铁桶试验预测工业焦炉成焦质量的研究%Prediction of the Coke Quality of Industrial Coke Oven Using Test Coke Oven

    Institute of Scientific and Technical Information of China (English)

    刘守军; 杨颂; 何小刚; 吕青

    2011-01-01

    为优化炼焦炉入炉煤配方以及提高焦炭产品质量,利用20 kg铁桶随炉试验以预测工业焦炉的成焦质量,并建立了预测数学模型.结果表明,利用20 kg铁桶试验可准确预测工业焦炉成焦强度,二者表现出很好的相关性,可直接用于指导工业生产过程中的配煤操作,具有很强的实用性.%In order to optimize coking coal blending and increase coke quality,a 20 kg test coke oven was adopted iuside industrial coke oven to predict the coke quality of industrial coke oven. A mathematical model was established for the prediction. Results show that the test coke oven predicted industrial coke oven accurately in coke quality with good correlation. Therefore,it is applicable to guiding coal blending for industrial production.

  10. Review On Automatic-Cleaning Basket Strainer

    Directory of Open Access Journals (Sweden)

    Deepak Gothwal

    2015-04-01

    Full Text Available 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 gets clogged a pressure difference is created between inlet amp outlet nozzle which is sensed by the differential pressure gauges. A differential pressure gauge activates backwash assembly which automatically cleans the strainer. Hence Self-Cleaning Basket Strainer is used to save cleaning time amp it automates the filtering process.

  11. Testing Stochastic Models for Simulating the Seeds Separation Process on the Sieves of a Cleaning System, and a Comparison with Experimental Data

    Directory of Open Access Journals (Sweden)

    Gheorghe Voicu

    2008-06-01

    Full Text Available A common method of analyzing experimental data is to determine the distributional model which best describes the process under study. In this paper, theoretical statistical models discussed by Tarcolea et al. (2008 are corroborated with data for the cleaning system of a combine harvester, data obtained experimentally in laboratory conditions. The purpose of this paper is to illustrate how some of the continuous distributions can be used for describing the variation separation intensity of seeds on sieve length. The Pearson coefficients show that some curves are far from the normal distribution, and better fits can be obtained with other distributions which can describe more adequately different degrees of skewness and peakedness of the curves. The considered probability laws are: normal, gamma, Weibull and beta distributions. The best results were obtained with gamma and beta distributions, since, for example, the values of the correlation coefficient R2 are in the most of the corresponding cases close to 1.

  12. 某发电厂EDTA清洗废水处理工艺改造%Process of a power plant EDTA cleaning wastewater treatment

    Institute of Scientific and Technical Information of China (English)

    彭佳佳

    2012-01-01

    随着发电机组扩建、发展,原废水处理系统已经不能满足电厂的要求,因此对废水处理工艺进行改造、扩建,以厌氧水解和接触氧化池代替活性污泥法,使EDTA化学清洗废水COD达到《污水综合排放标准》一级排放要求。%With the expansion of the generating units, the development of the original wastewater treatment system can not meet the requirements of the power plant, the wastewater treatment process to transform the expansion of anaerobic hydrolysis and exposure to oxidation ponds instead of activated sludge so that EDTA chemical cleaning COD of the integrated Wastewater Discharge Standard "an e- mission requirements.

  13. Petroleum Coke in the Urban Environment: A Review of Potential Health Effects

    OpenAIRE

    Caruso, Joseph A; Kezhong Zhang; Schroeck, Nicholas J.; Benjamin McCoy; McElmurry, Shawn P.

    2015-01-01

    Petroleum coke, or petcoke, is a granular coal-like industrial by-product that is separated during the refinement of heavy crude oil. Recently, the processing of material from Canadian oil sands in U.S. refineries has led to the appearance of large petcoke piles adjacent to urban communities in Detroit and Chicago. The purpose of this literature review is to assess what is known about the effects of petcoke exposure on human health. Toxicological studies in animals indicate that dermal or inh...

  14. Dry reforming of coke oven gases over activated carbon to produce syngas for methanol synthesis

    OpenAIRE

    Bermúdez Menéndez, José Miguel; Fidalgo Fernández, Beatriz; Arenillas de la Puente, Ana; Menéndez Díaz, José Ángel

    2010-01-01

    [EN] The dry reforming of coke oven gases (COG) over an activated carbon used as catalyst has been studied in order to produce a syngas suitable for methanol synthesis. The primary aim of this work was to study the influence of the high amount of hydrogen present in the COG on the process of dry reforming, as well as the influence of other operation conditions, such us temperature and volumetric hourly space velocity (VHSV). It was found that the reverse water gas shift (RWGS) reaction takes ...

  15. Proceedings of the Joint Meeting of The Fuel Society of Japan (1991). 28th Coal Science Conference/91st Coke Meeting; (Sha) nenryo kyokai godo taikai happyo ronbunshu (1991). Dai 28 kai sekitan kagaku kaigi dai 91 kai cokes tokubetsukai

    Energy Technology Data Exchange (ETDEWEB)

    1991-11-07

    Relating to coke, studies are made on the rapid coke production method, oven investigation during carbonization, and operational management/control. As to coal science, studies are mainly on the brown coal two-stage liquefaction (BCL) method, and data on the pilot plant and PSU are reported. Concerning bituminous coal liquefaction, PSU data mostly including the NEDOL process, and characteristics of liquefaction residue and its effective utilization by thermal decomposition are reported. Regarding the liquefaction mechanism, an experimentally extensive study on catalyst, solvent and reaction conditions is made using model materials and coal itself on the bench scale and also in the pilot plant. Engineering subjects on residue, solvent deashing, scale attachment and coprocessing are also reported. Relations of decomposition process to coal chemical structure changes and reaction conditions are investigated. As to coal gasification, studies, which are not many, are conducted on material balance, heat balance, and image characteristics of char for gasification and factors controlling reactivity.

  16. Implementation of a system of recovery of by-products for a coke oven pilot

    International Nuclear Information System (INIS)

    In this work is to the design of a lab-scale system that was constructed and started up to recover primary by-products of the coke gas, which in his first stage presents displays a mechanism of cooling made up of heat exchanger of double shell to reverse flow, a tower of perforated trays and a closed circuit of water that condenses tars. The second phase contemplates the entrance of the gas in crosscurrent to a tank divided by perforated trays with a permanent water shower, where the ammoniac solutions are concentrated. In order to avoid that the gas remains catches in the pipe of conduction by its high density, it is necessary to suck it by means of an extractor type snail closed, that acts as well like centrifugal separator precipitating the heaviest compounds, and impelling the gas towards a tower where the chemical cleaning of sulfurous and hydrocyanic compounds when reacting with the Lamming mixture takes place, providing a clean and ready gas for consumption. An experimental procedure is developed to test coals samples

  17. Plasma Spectral Analysis of Laser Cleaning Process in Air%空气中激光清洗过程的等离子体光谱分析

    Institute of Scientific and Technical Information of China (English)

    佟艳群; 张永康; 姚红兵; 孟春梅; 管海兵

    2011-01-01

    It is quick and accurate to on-line monitor the sample condition of laser cleaning by means of laser-induced plasma spectrum in air. In the present article, the echelle grating spectrometer was used to detect the plasma spectral lines induced by pulsed laser interaction with copper coin samples with or without contamination. The spectrogram showed that there were clear Cu I spectrum lines and air atom spectrum lines of N I and O I. In order to eliminate the uncertainty of single measurement, the statistical regularity of N I and OI spectrum lines was analyzed. Their intensity distribution laws were consistent and their relative standard deviations were the same basically. So a single measurement spectrum could be used to monitor cleaning process. The spectra of copper samples with contamination consisted of many elements atomic spectral lines and continuous spectral lines. But there are Cu I spectral lines in the spectra of clean copper samples. As a result, the authors could detect the change of spectral lines to judge whether the laser cleaning samples were clean.%在空气环境下,激光诱导等离子体光谱用于激光清洗状态的在线分析快速而准确.该文利用中阶梯光栅光谱仪探测脉冲激光器作用于干净及表面污染的铜币样品产生的等离子体光谱谱线,这些谱线中不但包含了清晰的铜原子发射谱线,还包含空气中氧气和氮气与激光作用产生分解效应的原子谱线.为了消除单次测量的不确定性,分析了多次测量的分布恒定的氧原子和氮原子谱线的统计规律,表明强度分布规律一致,且相对标准差基本相同,可以采用单次测量的光谱图变化表示清洗过程中状态.表面污染的铜币光谱图中包含多元素原子谱线和连续谱线,清洗干净铜币的光谱图连续谱线消失且只有铜元素谱线,观察谱线变化就可以表明样品是否被清洗干净.

  18. The Charfuel coal refining process

    International Nuclear Information System (INIS)

    The patented Charfuel coal refining process employs fluidized hydrocracking to produce char and liquid products from virtually all types of volatile-containing coals, including low rank coal and lignite. It is not gasification or liquefaction which require the addition of expensive oxygen or hydrogen or the use of extreme heat or pressure. It is not the German pyrolysis process that merely 'cooks' the coal, producing coke and tar-like liquids. Rather, the Charfuel coal refining process involves thermal hydrocracking which results in the rearrangement of hydrogen within the coal molecule to produce a slate of co-products. In the Charfuel process, pulverized coal is rapidly heated in a reducing atmosphere in the presence of internally generated process hydrogen. This hydrogen rearrangement allows refinement of various ranks of coals to produce a pipeline transportable, slurry-type, environmentally clean boiler fuel and a slate of value-added traditional fuel and chemical feedstock co-products. Using coal and oxygen as the only feedstocks, the Charfuel hydrocracking technology economically removes much of the fuel nitrogen, sulfur, and potential air toxics (such as chlorine, mercury, beryllium, etc.) from the coal, resulting in a high heating value, clean burning fuel which can increase power plant efficiency while reducing operating costs. The paper describes the process, its thermal efficiency, its use in power plants, its pipeline transport, co-products, environmental and energy benefits, and economics

  19. CLEAN Technique for Polarimetric ISAR

    Directory of Open Access Journals (Sweden)

    M. Martorella

    2008-01-01

    Full Text Available Inverse synthetic aperture radar (ISAR images are often used for classifying and recognising targets. To reduce the amount of data processed by the classifier, scattering centres are extracted from the ISAR image and used for classifying and recognising targets. This paper addresses the problem of estimating the position and the scattering vector of target scattering centres from polarimetric ISAR images. The proposed technique is obtained by extending the CLEAN technique, which was introduced in radar imaging for extracting scattering centres from single-polarisation ISAR images. The effectiveness of the proposed algorithm, namely, the Polarimetric CLEAN (Pol-CLEAN is tested on simulated and real data.

  20. Mini-PROven. Reduced emissions from small and medium-size coke ovens thanks to single-chamber pressure control; Mini-PROven. Emissionsreduzierung an kleinen und mittleren Koksoefen mit einer Einzelkammerdruckregelung

    Energy Technology Data Exchange (ETDEWEB)

    Huhn, Friedrich; Krebber, Frank; Kuehn-Gajdzik, Joanna; Ueberschaer, Kerstin [ThyssenKrupp Uhde GmbH, Dortmund (Germany). Coke Plant Technologies Div.

    2012-07-01

    For environment and occupational health reasons it is becoming increasingly important for coke plants to be operated with the lowest possible level of emissions. In the past, changing pressure conditions in each individual oven, with particularly high values at the beginning of the coking period, often resulted in considerable emissions at the oven closures. To prevent this happening on modern large-scale ovens, ThyssenKrupp Uhde developed the PROven trademark (Pressure Regulated Oven), a single-chamber pressure control system which regulates the pressure in the individual coke chambers down to a constantly low level. In the meantime, after many years of successful service, the system has been upgraded in both its design and process engineering. The result is Mini-PROven, which in future can also be retro-fitted to old small and medium-size coke oven batteries in the interest of better environmental protection. (orig.)