Relevant bibliographies by topics / Coke – Combustion

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  1. Journal articles
  2. Dissertations / Theses
  3. Books
  4. Book chapters
  5. Conference papers
  6. Reports

Academic literature on the topic 'Coke – Combustion'

Author: Grafiati
Published: 4 June 2021
Last updated: 8 February 2022

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Journal articles on the topic "Coke – Combustion"

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Nyakuma, Bemgba, Olagoke Oladokun, and Aliyu Bello. "Combustion Kinetics of Petroleum Coke by Isoconversional Modelling." Chemistry & Chemical Technology 12, no. 4 (December 10, 2018): 505–10. http://dx.doi.org/10.23939/chcht12.04.505.

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Cheng, C. L. "Coke oven gas combustion systems." Fuel and Energy Abstracts 37, no. 3 (May 1996): 204. http://dx.doi.org/10.1016/0140-6701(96)88856-4.

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Wang, Ziming, Ko-ichiro Ohno, Shunsuke Nonaka, Takayuki Maeda, and Kazuya Kunitomo. "Temperature Distribution Estimation in a Dwight–Lloyd Sinter Machine Based on the Combustion Rate of Charcoal Quasi-Particles." Processes 8, no. 4 (March 31, 2020): 406. http://dx.doi.org/10.3390/pr8040406.

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The coke combustion rate in an iron ore sintering process is one of the most important determining factors of quality and productivity. Biomass carbon material is considered to be a coke substitute with a lower CO2 emission in the sintering process. The purpose of this study was to investigate the combustion rate of a biomass carbon material and to use a sintering simulation model to calculate its temperature profile. The samples were prepared using alumina powder and woody biomass powder. To simplify the experimental conditions, alumina powder, which cannot be reduced, was prepared as a substitute of iron ore. Combustion experiments were carried out in the open at 1073 K~1523 K. The results show that the combustion rates of the biomass carbon material were higher than that of coke. The results were analyzed using an unreacted core model with one reaction interface. The kinetic analysis found that the kc of charcoal was higher than that of coke. It is believed that the larger surface area of charcoal may affect its combustion rate. The analysis of the sintering simulation results shows that the high temperature range of charcoal was smaller than that of coke because of charcoal’s low fixed carbon content and density.
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Yang, Guisheng, Zhihong Yang, Jinliang Zhang, Zhanhai Yang, and Jiugang Shao. "Combustion Characteristics and Kinetics Study of Pulverized Coal and Semi-Coke." High Temperature Materials and Processes 38, no. 2019 (February 25, 2019): 783–91. http://dx.doi.org/10.1515/htmp-2019-0034.

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AbstractCombustion process of bituminous coal, steam coal, anthracite (AC) and semi-coke were investigated through thermogravimetric analysis method and influence of metamorphic grade as well as heating rate on combustion characteristics were analyzed. Results show that combustion performance could not be represented by single combustion characteristic parameter. Through analysis of comprehensive combustion characteristic indexes, with increase of metamorphic grade combustion performance of coal is lowered, and combustion performance of semi-coke and AC are close to each other. With increase of heating rate, combustion curves move into high temperature region and comprehensive combustion characteristic indexes are increased, which show that the combustion performance is improved. Random pore model (RPM), unreacted shrinking core model (URCM) and volume model were used to calculate kinetic parameters of combustion process. Results show that RPM has the best performance to represent combustion process of the four samples and through calculation by RPM kinetic energy of combustion process for all samples are between 43.08 and 99.43 kJ/mol, and there is compensation effect during combustion process.
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Brandauer, M., A. Schulz, and S. Wittig. "Mechanisms of Coke Formation in Gas Turbine Combustion Chambers." Journal of Engineering for Gas Turbines and Power 118, no. 2 (April 1, 1996): 265–70. http://dx.doi.org/10.1115/1.2816587.

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New gas turbine combustor designs are developed to reduce pollutant and NOx emissions. In these new combustors, the formation of carbonaceous deposits, especially in prevaporizers, affects the reliability and effectiveness of operation. To avoid deposits, a detailed knowledge of the origins and mechanisms of formation is required. To obtain a deeper insight, the phenomena were studied systematically. The deposits under consideration show differing characteristics suggesting more than one formation mechanism in the combustor. Consequently, the primary goal was to identify the formation mechanisms and, subsequently, to simulate the mechanisms under well-defined conditions in bench tests for determining the relevant parameters of deposit build-up. The mechanisms of formation were identified based on the properties of the deposits in the combustion chamber. In order to characterize the deposits, physical and chemical analysis techniques were utilized. In summary, tests and numerical predictions identified two major paths of formation: a deposit build-up resulting from flame products such as soot or coked droplets and a deposit build-up resulting from liquid fuel impinging the wall accompanied with chemical reactions at the wall. The deposits caused by fuel droplet impingement were intensively studied in bench tests. In analyzing the processes, the influence of wall temperature, fuel composition, and the oxygen content in the environment is shown in detail. In addition, the importance of thermal instabilities of the fuel, previously studied under fuel supply system conditions, is demonstrated for a deposit formation inside a combustion chamber.
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Kou, Luyao, Junjing Tang, Tu Hu, Baocheng Zhou, and Li Yang. "Effect of CaO on catalytic combustion of semi-coke." Green Processing and Synthesis 10, no. 1 (January 1, 2021): 011–20. http://dx.doi.org/10.1515/gps-2021-0002.

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Abstract Generally, adding a certain amount of an additive to pulverized coal can promote its combustion performance. In this paper, the effect of CaO on the combustion characteristics and kinetic behavior of semi-coke was studied by thermogravimetric (TG) analysis. The results show that adding proper amount of CaO can reduce the ignition temperature of semi-coke and increase the combustion rate of semi-coke; with the increase in CaO content, the combustion rate of semi-coke increases first and then decreases, and the results of TG analysis showed that optimal addition amount of CaO is 2 wt%. The apparent activation energy of CaO with different addition amounts of CaO was calculated by Coats–Redfern integration method. The apparent activation energy of semi-coke in the combustion reaction increases first and then decreases with the increase in CaO addition. The apparent activation energies of different samples at different conversion rates were calculated by Flynn–Wall–Ozawa integral method. It was found that the apparent activation energies of semi-coke during combustion reaction decreased with the increase in conversion.
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KONG, Dejuan, Yong WANG, Qulan ZHOU, Na LI, Yuhua LI, Tongmo XU, and Shien HUI. "B210 COMPARATIVE STUDY ON COMBUSTION PERFORMANCE OF PETROLEUM COKE, HEJIN COAL AND SHENMU COAL(Combustion-6)." Proceedings of the International Conference on Power Engineering (ICOPE) 2009.2 (2009): _2–135_—_2–139_. http://dx.doi.org/10.1299/jsmeicope.2009.2._2-135_.

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Vossoughi, Shapour, and Youssef El-Shoubary. "Kinetics of Crude-Oil Coke Combustion." SPE Reservoir Engineering 4, no. 02 (May 1, 1989): 201–6. http://dx.doi.org/10.2118/16268-pa.

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Miroshnichenko, I. V., D. V. Miroshnichenko, I. V. Shulga, and Y. S. Balaev. "THE FORECAST OF COKE COMBUSTION HEAT." Journal of Coal Chemistry 2 (February 2020): 11–21. http://dx.doi.org/10.31081/1681-309x-2020-0-2-11-21.

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OKSANEN, A., and R. KARVINEN. "Combustion-Generated NOxand Coke in Heavy Residual Fuel Oil Combustion." Combustion Science and Technology 108, no. 4-6 (January 1995): 345–61. http://dx.doi.org/10.1080/00102209508960406.

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Dissertations / Theses on the topic "Coke – Combustion"

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Witzel, Lars. "Formation d’imbrûlés solides lors de la combustion des fuels lourds." Lyon, INSA, 1993. http://www.theses.fr/1993ISAL0028.

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Les préoccupations environnementales amènent à des limites réglementaires d'émission de plus en plus sévères pour la combustion des fuels lourds. Notre objectif est de déterminer les possibilités de prédiction des imbrûlés solides émis par les chaudières industrielles. Dans un premier temps, des gouttelettes de fuel lourd sont pyrolysées dans un tube à chute en milieu inerte pour obtenir des particules solides (des sphères creuses appelées cénosphères). Le rapport massique, cénosphères/fuel injecté est établi. Dans un deuxième temps la réactivité à l'air est mesurée par analyse thermogravimétrique. Les résultats obtenus (rapport massique cénosphères/fuel injecté, réactivité et température d’inflammation des cénosphères peuvent suffire pour assurer le suivi d'une production d'un fuel et pour tester l'efficacité d'un additif de combustion. Un modèle de simulation de la pyrolyse rapide d'une gouttelette de fuel lourd et de la formation d'une particule solide a été développé
An enforced conscience toward the environment led too stricter emission limit regulations for the combustion of heavy fuel oil. This work is ta determine the possibilities for the prediction of solid emissions of industrial plants. In a first step fuel oil droplets are pyrolysed in inert gas while falling down a tube , to obtain solid particles (hollow spheres, called cenospheres). The mass ratio cenospheres/injected fuel is established. In a second step, the reactivity with air is measured by thermogravimetric analysis. The results (mass ratio cenospheres/fuel, reactivity and ignitions temperature of the cenospheres) may be sufficient to control the quality of one heavy fuel oil production and to test the efficiency of combustion additives. A model that simulates the fast pyrolysis of a heavy fuel oil droplet and the particle formation has been developed
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Prieto, Jiménez Natalia. "Simulação da combustão de coque em regeneradores FCC usando fluidodinâmica computacional." [s.n.], 2011. http://repositorio.unicamp.br/jspui/handle/REPOSIP/266866.

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Orientador: Milton Mori
Dissertação (mestrado) - Universidade Estadual de Campinas, Faculdade de Engenharia Química
Made available in DSpace on 2018-08-18T19:12:31Z (GMT). No. of bitstreams: 1 PrietoJimenez_Natalia_M.pdf: 6938239 bytes, checksum: 6c44d3053179a676042ac55971eeb06b (MD5) Previous issue date: 2011
Resumo: Craqueamento Catalítico Fluidizado (FCC) é um processo amplamente utilizado para converter frações de hidrocarbonetos de óleos brutos de petróleo com elevado ponto de ebulição, a produtos mais valiosos tais como gasolina e gases olefínicos (alcenos). Durante as reações de craqueamento, o catalisador é desativado rapidamente devido à deposição de coque na sua superfície. Em unidades industriais de FCC, o catalisador desativado é continuamente regenerado utilizando um regenerador, conectado ao reator riser. Além da regeneração do catalisador (combustão de coque pelo contato com o ar), o regenerador FCC fornece também a energia necessária para as reações de craqueamento endotérmicas. O objetivo deste trabalho de pesquisa é simular a combustão de coque em um regenerador tridimensional, analisado variáveis de saída como concentração de carbono, temperatura, velocidade axial e radial das fases sólida e gasosa, e fração volumétrica de sólidos, mediante a técnica de Fluidodinâmica Computacional (CFD). Para isto, são utilizadas duas configurações de regenerador com dimensões e condições de contorno tomadas da literatura. Para a modelagem matemática e numérica utilizaram-se os softwares comerciais ANSYS-CFX V11 e FLUENT V12, junto com sub-rotinas desenvolvidas durante a pesquisa. Foram comparados sistemas de reação homogênea e heterogênea utilizando o modelo cinético Finite-Rate laminar, no qual as taxas de reação são determinadas pelas expressões cinéticas de Arrhenius. Do desenvolvimento das simulações obtiveram-se resultados satisfatórios que serão úteis no entendimento do complexo processo da regeneração de catalisadores para processos de FCC
Abstract: Fluidized Catalytic Cracking (FCC) is a widely used process to convert hydrocarbon fractions of crude petroleum oils with high boiling point to more valuable products such as gasoline and olefin gases (alkenes). During the cracking reactions, the catalyst is quickly deactivated due to coke deposition on its surface. In FCC industrial units, deactivated catalyst is continuously regenerated using a regenerator, connected to the riser reactor. In addition to catalyst regeneration (coke combustion by contact with air), FCC regenerator also provides the necessary energy for endothermic cracking reactions. The aim of this research was to simulate the coke combustion in a three-dimensional regenerator, analyzing output variables as coke concentration, temperature, axial and radial velocity of solid and gaseous phases, and solid volume fraction through the technique of Computational Fluid Dynamics (CFD). For this purpose two configurations of regenerator were used with dimensions and boundary conditions taken from the literature. For mathematical and numerical modeling, the commercial software ANSYS-CFX V11 and FLUENT V12 were used, with subroutines developed during the research. Homogeneous and heterogeneous reaction systems were compared using the laminar Finite-Rate kinetic model, in which the reaction rates are determined by Arrhenius kinetic expressions. The simulation of this system produced satisfactory results that will be useful in understanding the complex process of catalyst regeneration for FCC processes
Mestrado
Desenvolvimento de Processos Químicos
Mestre em Engenharia Química
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Radhakrishnan, Arun. "Self-sustained combustion of low grade solid fuels in a stagnation-point reverse-flow combustor." Diss., Georgia Institute of Technology, 2013. http://hdl.handle.net/1853/50275.

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This thesis investigates the use of the Stagnation-Point Reverse-Flow (SPRF) combustor geometry for burning low-grade solid fuels that are attractive for specific industrial applications because of their low cost and on-site availability. These fuels are in general, hard to burn, either because of high moisture and impurity-content, e.g. biomass, or their low-volatiles content, e.g., petroleum-coke. This results in various challenges to the combustor designer, for example reduced flame stability and poor combustion efficiency. Conventional solutions include preheating the incoming flow as well as co-firing with high-grade fuels. The SPRF combustor geometry has been chosen because it was demonstrated to operate stably on standard gaseous and liquid-fuels corresponding to ultra fuel-lean conditions and power densities at atmospheric-pressure around 20-25 MW/m3. Previous studies on the SPRF combustor have proven that the unique, reverse flow-geometry allows entrainment of near-adiabatic products into the incoming reactants, thereby enhancing the reactivity of the mixture. Further, the presence of the stagnation-end created a region of low mean velocities and high levels of unsteadiness and mixing-rates that supported the reaction-zones. In this study, we examine the performance of the SPRF geometry on a specific low grade solid fuel, petroleum coke. There are three main goals of this thesis. The first goal is the design of a SPRF combustor to operate on solid-fuels based on a design-scaling methodology, as well as demonstration of successful operation corresponding to a baseline condition. The second goal involves understanding the mode of operation of the SPRF combustor on solid-fuels based on visualization studies. The third goal of this thesis is developing and using reduced-order models to better understand and predict the ignition and quasi-steady burning behavior of dispersed-phase particles in the SPRF combustor. The SPRF combustor has been demonstrated to operate stably on pure-oxygen and a slurry made from water and petroleum-coke, both at the baseline conditions (125 kW, 18 g/s, ~25 µm particles) and higher power-densities and powder sizes. For an overall combustor length less than a meter, combustion is not complete (global combustion efficiency less than 70%). Luminance imaging results indicate the incoming reactant jet ignites and exhibits intense burning at the mid-combustor region, around 15 jet diameters downstream of the inlet, most likely due to enhanced mixing as a result of the highly unsteady velocity field. This roughly corresponds to the location of the reaction zones in the previous SPRF combustors operating on gas and liquid fuels. Planar laser visualization of the reacting flow-field using particle-scattering reveals that ignition of a significant amount of the reactants occurs only after the incoming jet has broken into reactant packets. Post-ignition, these burning packets burn out slowly as they reverse direction and exit the combustor on either side of the central injector. This is unlike the behavior in liquid and gas-fueled operation where the incoming reactants burned across a highly corrugated, thin-flame front. Based on these findings, as well as the results of previous SPRF studies, an idealized model of combustor operation based on a plug flow reactor has been developed. The predictions suggest that fuel-conversion efficiency is enhanced by the combustor operating pressure and lowered by the heat-losses. Overall, this effort has shown the SPRF geometry is a promising compact-combustor concept for self-sustained operation on low-grade solid-fuels for typical high-pressure applications such as direct steam-generation. Based on these findings, it is recommended that future designs for the specific application previously mentioned have a shorter base-combustor with lower heat-losses and a longer steam-generation section for injection of water.
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Simard, Guy. "La modélisation de la combustion dans un four de calcination de coke de pétrole /." Thèse, Chicoutimi : Université du Québec à Chicoutimi, 1992. http://theses.uqac.ca.

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Omar, Faisal. "Contribution à l'étude de la gazéification et de la combustion des combustibles solides." Aix-Marseille 3, 1986. http://www.theses.fr/1986AIX30031.

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L'étude de la vapogazéification et de la combustion des combustibles solides (cokes de charbon, cokes de pétrole) a été effectuée à l'aide d'un petit réacteur à lit fixe et d'un ordinateur de procédé qui traite les signaux en temps réel. On a pu montrer ainsi qu'un modèle semi-empirique simple : le modèle du rétrécissement non uniforme permet de définir la réactivité intrinsèque et l'accélération du rétrécissement. Ce modèle caractérise le comportement de la particule unique non seulement en l'absence de freinages thermiques et diffusionnels, mais également, dans une certaine mesure, lorsque ces transferts interviennent. Le réacteur à lit circulant de vapogazéification peut être à la fois modélisé et simulé. On a montré que ce nouveau type de réacteur permet d'obtenir des rendements élevés dans des conditions de fonctionnement relativement peu sévères.
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Zhao, Lei. "Simulation of Combustion and Thermal-flow Inside a Pyroscrubber." ScholarWorks@UNO, 2008. http://scholarworks.uno.edu/td/863.

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The main function of a pyroscrubber in petroleum coke calcining process is to oxidize the carbonaceous contents, including hydrocarbon volatiles, of the exhaust gas from the calcination kiln, so as to leave no more than small traces of unburned volatiles, solid carbon, ashes, or emissions (e.g. CO, NOx and SOx) in the flue gas finally discharged. To maximize the energy recovery and reduce pollutant emission from the pyroscrubber, 3-D computational models are developed using FLUENT to simulate the combustion and thermal-flow phenomena inside the pyroscrubber. The results show the 3-D behavior of the flow, the reaction inside the pyroscrubber, effect of different amounts of air injection with respect to combustion efficiency, energy output and NOx emission. A multistage burning strategy is introduced and studied and results show it successfully cuts emission without compromising energy output. A particle combustion model with the homogeneous gas combustion model is also developed and incorporated to investigate CO emission.
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Linn, Nyein Nyein [Verfasser]. "Combustion behavior of lumpy coke particle under shaft kiln conditions / Nyein Nyein Linn." Magdeburg : Universitätsbibliothek, 2017. http://d-nb.info/1158660103/34.

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Zhang, Zexuan. "Simulation of Combustion and Thermal-flow Inside a Petroleum Coke Rotary Calcining Kiln." ScholarWorks@UNO, 2007. http://scholarworks.uno.edu/td/1073.

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Calcined coke is the best material for making carbon anodes for smelting of alumina to aluminum. Calcining is an energy intensive industry and a significant amount of heat is wasted in the calcining process. Efficiently managing this energy resource is tied to the profit margin and survivability of a calcining plant. 3-D computational models are developed using FLUENT to simulate the calcining process inside the long slender kiln. Simplified models are employed to simulate the moving petocke bed with a uniform distribution of moisture evaporation, devolatilization, and coke fines entrainment rate with a conjugate radiation-convection-conduction calculation. The results show the 3-D behavior of the flow, the reaction inside the kiln, heat transfer and the effect of the tertiary air on coke bed heat transfer. The ultimate goals are to reduce energy consumption, recover waste-heat, increase thermal efficiency, and increase the product yield.
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Edeki, Onoriode Lucky. "Fundamental investigations into the effects of different plastic wastes stream on both coke quality and products combustion." Thesis, University of Nottingham, 2007. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.486870.

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Plastic waste recycling still remains a major challenge in environmental protection despite available different routes such as emerging mechanical, chemical, and energy recycling. Recently, the addition of wastes plastics as minor components of coal blends for metallurgical coke manufacturing has been proposed. This thesis explores the modification of the thermoplastic properties of coal in order to assess the possibility of blending plastic wastes with coal for the production of metallurgical coke and the' usefulness of the by products. A bitumininous coal K6 was used as a base component of blends with different plastic products such as polyethylene (PE), polystyrene (PS), poly (ethylene terephthalate) (PET), flexible polyurethane (FPU), and car shredder fluff (CSF).
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Duretz, Marc. "La combustion dans le four water-jacket à plomb : influence des caractéristiques du coke et des paramètres de conduite." Châtenay-Malabry, Ecole centrale de Paris, 1989. http://www.theses.fr/1989ECAP0240.

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Les performances du haut fourneau à plomb water-jacket sont limitées principalement par le rendement du transfert thermique du gaz vers la charge, et sont notamment très sensibles aux modalités de la combustion du coke. Or, des investigations menées dans les fours de la société METALEUROP (ex-PENARROYA) ont révélé des fluctuations incontrôlées de leur fonctionnement thermique. Nous cherchons à comprendre ces phénomènes pour aider à les maitriser. Nous mettons d'abord en évidence les régimes de diffusion qui gouvernent la gazéification d'un grain de coke dans le four à plomb, et qui font du calibre du coke son critère primordial de qualité. Puis, par des expériences de combustion à échelle 1, nous dressons les cartes de compositions du gaz et de température dans le massif de coke irrigue par une tuyère du Water-Jacket. Nous précisons le rôle des paramètres géométriques et aérodynamiques, dont l'influence masque couramment celle de la réactivité chimique du coke. Enfin, nous examinons par une simulation numérique les relations entre la combustion du coke et le transfert thermique dans le four a plomb. Nous analysons l'influence des caractéristiques du coke et des paramètres de conduite de la marche industrielle sur les performances du four (productivité, mise au mille, températures des produits de coulée et du gaz de gueulard). Nos conclusions concernent les critères et tests de qualité du coke, et la conduite du Water-Jacket. À cote du test actuel de réactivité du coke, nous proposons un test granulométrique et de résistance mécanique pour juger l'opportunité du criblage. Concernant la conduite du four, nous suggérons plusieurs voies d'amélioration: guidage des paramètres opératoires par le suivi en continu, chargement du coke tirant parti de la ségrégation granulométrique, réglage de la répartition du vent aux tuyères
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Books on the topic "Coke – Combustion"

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Symposium on "Coke Properties Required by the Blast Furnace for Stable Operation" (1989 Hamilton, Ont.). Coke properties required by the blast furnace for stable operation: Proceedings of the Symposium on "Coke Properties Required by the Blast Furnace for Stable Operation". Hamilton, Ont., Canada: Dept. of Materials Science and Engineering, McMaster University, 1989.

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Shavit, Zeev. Using PHOENICS computer code for transient one-dimensional metal combustion in steam. Monterey, Calif: Naval Postgraduate School, 1986.

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Inspectorate, Great Britain Fire Service. Dangerous goods emergency action code list 2005. 2nd ed. London (UK): Stationery Office, 2005.

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Cramond, Wallis R. Shutdown decay heat removal analysis of a combustion engineering 2-loop pressurized water reactor: Case study. Washington, DC: Division of Reactor and Plant Systems, Office of Nuclear Regulatory Research, U.S. Nuclear Regulatory Commission, 1987.

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Bickford, W. E. Effects of control system failures on transients, accidents, and core-melt frequencies at a combustion engineering pressurized water reactor. Washington, D.C: Division of Risk Anlaysis and Operations, Office of Nuclear Regulatory Research, U.S. Nuclear Regulatory Commission, 1986.

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Bickford, W. E. Effects of control system failures on transients, accidents, and core-melt frequencies at a combustion engineering pressurized water reactor. Washington, D.C: Division of Risk Anlaysis and Operations, Office of Nuclear Regulatory Research, U.S. Nuclear Regulatory Commission, 1986.

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Sullivan, Timothy J. Evaluation of a Stirling engine heater bypass with the NASA Lewis nodal-analysis performance code. Cleveland, Ohio: National Aeronautics and Space Administration, Lewis Research Center ; [Springfield, Va., 1986.

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Williams, Donald Charles. Mitigation of direct containment heating and hydrogen combustion events in ice condenser plants: Analyses with the CONTAIN code and NUREG-1150 PRA methodology. Washington, DC: Division of Safety Issue Resolution, Office of Nuclear Regulatory Research, U.S. Nuclear Regulatory Commission, 1990.

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Hutchinson, Bobby. Spontaneous Combustion: Code Red - 1. Harlequin, 2004.

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Vaidyanathan, Sankaran, Stone Christopher, and NASA Glenn Research Center, eds. Subgrid combustion modeling for the next generation national combustion code. [Cleveland, Ohio]: National Aeronautics and Space Administration, Glenn Research Center, 2003.

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Book chapters on the topic "Coke – Combustion"

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Prado, G., D. Froelich, and J. Lahaye. "Heterogeneous Combustion of Residual Coke Particle." In Fundamentals of the Physical-Chemistry of Pulverized Coal Combustion, 219–41. Dordrecht: Springer Netherlands, 1987. http://dx.doi.org/10.1007/978-94-009-3661-4_9.

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Vejahati, Farshid, and Rajender Gupta. "Co-Gasification of Oil Sand Coke with Coal." In Cleaner Combustion and Sustainable World, 917–23. Berlin, Heidelberg: Springer Berlin Heidelberg, 2012. http://dx.doi.org/10.1007/978-3-642-30445-3_124.

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Park, Myung Ho, and Dae Yong Shin. "The Combustion Characteristics of Refuse Derived Fuels Using Coke/Waste Tire." In Materials Science Forum, 265–68. Stafa: Trans Tech Publications Ltd., 2005. http://dx.doi.org/10.4028/0-87849-966-0.265.

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Lin, L. S., C. S. Zhao, S. Wang, G. Zhu, and W. G. Xiang. "Characteristics of Catalytic Gasification of Natural Coke with H2O in a Fluidized Bed." In Proceedings of the 20th International Conference on Fluidized Bed Combustion, 732–39. Berlin, Heidelberg: Springer Berlin Heidelberg, 2009. http://dx.doi.org/10.1007/978-3-642-02682-9_113.

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Su, Bo, Sheng-li Wu, Guo-liang Zhang, Zhi-gang Que, and Chao-gang Hou. "Influence of Coke Breeze Combustion Conditions on the Emission of NOx in Sintering Process." In 6th International Symposium on High-Temperature Metallurgical Processing, 387–94. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2015. http://dx.doi.org/10.1002/9781119093381.ch49.

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Su, Bo, Sheng-li Wu, Guo-liang Zhang, Zhi-gang Que, and Chao-gang Hou. "Influence of Coke Breeze Combustion Conditions on the Emission of NOx in Sintering Process." In 6th International Symposium on High-Temperature Metallurgical Processing, 387–94. Cham: Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-48217-0_49.

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Armbruster, Wolfgang, Justin S. Hardi, and Michael Oschwald. "Experimental Investigation of Injection-Coupled High-Frequency Combustion Instabilities." In Notes on Numerical Fluid Mechanics and Multidisciplinary Design, 249–62. Cham: Springer International Publishing, 2020. http://dx.doi.org/10.1007/978-3-030-53847-7_16.

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Abstract Self-excited high-frequency combustion instabilities were investigated in a 42-injector cryogenic rocket combustor under representative conditions. In previous research it was found that the instabilities are connected to acoustic resonance of the shear-coaxial injectors. In order to gain a better understanding of the flame dynamics during instabilities, an optical access window was realised in the research combustor. This allowed 2D visualisation of supercritical flame response to acoustics under conditions similar to those found in European launcher engines. Through the window, high-speed imaging of the flame was conducted. Dynamic Mode Decomposition was applied to analyse the flame dynamics at specific frequencies, and was able to isolate the flame response to injector or combustion chamber acoustic modes. The flame response at the eigenfrequencies of the oxygen injectors showed symmetric and longitudinal wave-like structures on the dense oxygen core. With the gained understanding of the BKD coupling mechanism it was possible to derive LOX injector geometry changes in order to reduce the risks of injection-coupled instabilities for future cryogenic rocket engines.
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Seddougui, Sharon O. "Stability of Hypersonic Flow Over a Cone." In Transition, Turbulence and Combustion, 245–54. Dordrecht: Springer Netherlands, 1994. http://dx.doi.org/10.1007/978-94-011-1032-7_22.

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Pruett, C. David, and Chau-Lyan Chang. "Transitional High-Speed Flow on a Cone: PSE Versus DNS." In Transition, Turbulence and Combustion, 379–89. Dordrecht: Springer Netherlands, 1994. http://dx.doi.org/10.1007/978-94-011-1032-7_37.

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Cachier, Hélène. "Combustion Carbonaceous Aerosols in the Atmosphere: Implications for Ice Core Studies." In Ice Core Studies of Global Biogeochemical Cycles, 313–46. Berlin, Heidelberg: Springer Berlin Heidelberg, 1995. http://dx.doi.org/10.1007/978-3-642-51172-1_17.

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Conference papers on the topic "Coke – Combustion"

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Vossoughi, S., and Y. EI-Shoubary. "Kinetics of Crude Oil Coke Combustion." In SPE International Symposium on Oilfield Chemistry. Society of Petroleum Engineers, 1987. http://dx.doi.org/10.2118/16268-ms.

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Zhao, Changsui, Wenxuan Wang, Fengjun Wang, Chuanmin Chen, and Song Han. "Emission Control of Gaseous Pollutants From Co-Firing of Petroleum Coke and Coal in CFB." In 17th International Conference on Fluidized Bed Combustion. ASMEDC, 2003. http://dx.doi.org/10.1115/fbc2003-103.

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Petroleum cokes including delayed coke, fluid coke, etc. are byproducts of solid residuals from the crude refining process. Using high sulfur petroleum coke as alternative fuel is feasible owing to its high fixed carbon and low ash content, but petroleum cokes are difficult to ignite due to their low volatile content and containing substantial concentrations of vanadium, nickel, nitrogen and sulfur, which can be sources of pollution emission and fireside fouling or corrosion problem. Co-firing petroleum coke and coal in circulating fluidized bed (CFB) is an ideal solution for those problems. Emission characteristic of gaseous pollutants from co-firing petroleum coke and coal is investigated in the paper. Experiments were carried out in a 0.6 MWt pilot-scale CFB combustor with the total height of 12m from the air distributor to the exit of combustor. The concentrations of SO2, NO, N2O, O2, CO2 and CO were measured on line by the gas analyzer. The effect of several parameters, in term of the primary air percentage, air excess coefficient, bed temperature, Ca/S molar ratio and percentage of petroleum coke in mixed fuel on the emission of SO2, NO, N2O is verified in experiments. Experimental results show that SO2 concentration in flue gas reduces with increase in the primary air percentage, excess air coefficient and Ca/S ratio for all kinds of fuel mixtures, whereas NO, N2O concentration rises with increase in the primary air percentage and excess air. When the bed temperature changes, the NO concentration varying trend is opposite to N2O. There is an optimal temperature for sulfur retention. Co-firing of petroleum coke and coal with different mixing ratio in CFB can be stable, efficient and environment friendly.
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Zhao, Changsui, Chuanmin Chen, Xiaoping Chen, Fengjun Wang, Wenxuan Wang, Aiqiang Zhu, and Xin Wu. "Experimental Study on Characteristics of Pyrolysis, Ignition and Combustion of Blends of Petroleum Coke and Coal in CFB." In 18th International Conference on Fluidized Bed Combustion. ASMEDC, 2005. http://dx.doi.org/10.1115/fbc2005-78048.

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It is a common understanding that co-firing of petroleum coke and coal in circulating fluidized bed (CFB) is an efficient, economical and environment-friendly way to utilize petroleum coke with medium or high sulfur content. Experimental investigations on characteristics of pyrolysis, ignition and combustion of petroleum coke, coal and their blends with different mixing ratios were conducted on a thermogravimetric analyzer and a pilot CFB combustor systematically. Ignition temperature and burnout temperature were also acquired. The effects of several parameters in terms of the fuel category, the heating rate, the coal/coke mass flow ratio, the CO2 partial pressure, and the Ca/S molar ratio on the ignition and burnout characteristics of the petroleum coke and the blends of the petroleum coke and coal were verified. The results show that the ignition temperature and the burnout temperature of the petroleum coke are between those of bituminous coal and anthracite, which implies that its combustion characteristic is between bituminous coal and anthracite, but is more closer to the bituminous. The pyrolysis process of blends of petroleum coke and coal accords with mechanism model (1−α)1.5 well, and the combustion process accords with mechanism model w1.5 well. Although the ignition temperature of the blended fuels keeps the same when the heating rate, or the CO2 partial pressure or the Ca/S molar ratio increases, the burnout temperature decreases gradually. With decrease in the coal/coke mass flow ratio, the ignition temperature and the burnout temperature of the blends rise.
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Zhang, Chun-Lin, Gui-Cheng Yuan, De-Chang Liu, Han-Ping Chen, Ding-Yu Liu, and Rong Wang. "An Experimental Study of the Gaseous Pollution Emissions in Petroleum-Coke-Fired Fluidized Beds." In 17th International Conference on Fluidized Bed Combustion. ASMEDC, 2003. http://dx.doi.org/10.1115/fbc2003-030.

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Petroleum cokes have high calorific value (about 37 MJkg−1), high sulfur content (2–7% wt.), and high nitrogen content (1∼3% wt.), introducing serious environmental problems when using as fuel. In this paper the effects of operating parameters (bed temperature, Ca/S mole ratio, and excess oxygen) on gaseous pollutant (SO2, NO, and N2O) emissions in a well-controlled bench scale fluidized bed reactor and an 1t/h bubbling fluidized bed for different type of petroleum cokes. Finally, the pollution emission differences between petroleum coke and coal were compared and the reasons were analyzed.
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Le Guevel, Thierry, and Philippe Thomas. "Fuel Flexibility and Petroleum Coke Combustion at Provence 250 MW CFB." In 17th International Conference on Fluidized Bed Combustion. ASMEDC, 2003. http://dx.doi.org/10.1115/fbc2003-094.

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The Provence 250 MWe CFB boiler was originally designed in 1992 for a local coal (Provence lignite) with a high sulfur and high ash content. This large CFB, features a pant leg bottom furnace, 4 cyclones and 4 fluid bed heat exchangers to provide the active temperature control of the furnace and reheated steam final temperature. After start up in 1995 with this local coal, several other fuel types were burnt. Mainly 3 fuels were tested over the last 5 years, on a long term basis, with various degrees of combination with the Gardanne coal up to full firing alone: • a lean coal (Gard, France), low volatile bituminous type, not far from semi anthracite type coals, • an imported coal, representative of low ash low sulfur content imported coal, • a petroleum coke, with a high sulfur content. This last test demonstrates the widest flexibility with regards to fuel reactivity range of a CFB plant with this architecture. The fuel, limestone and ash handling/injection systems were able to cope with this fuel diversity without equipment modifications. Since these tests were conclusive both on the pollutant emissions and on the operating concern, a permit to burn petroleum coke in commercial operation in a 250 MWe CFB boiler has been obtained in December 2001. This paper presents the main features and the results of the petroleum coke tests performed and compare them with the feedback on operating conditions of the boiler and emissions performances for Provence lignite and imported coal. These positive results demonstrate the wide fuel capability of large CFB boilers with this boiler architecture. First, they emphasize the critical role of advanced cyclones to accept fuels with very different reactivities and minimize limestone consumption. Second, these results show the role of the Fluid Bed Heat Exchangers system to control actively the furnace temperature, while controlling the reheated steam temperature without using spray.
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Wang, Jinsheng, Edward J. Anthony, and J. Carlos Abanades. "A Simulation Study for Fluidized Bed Combustion of Petroleum Coke With CO2 Capture." In 17th International Conference on Fluidized Bed Combustion. ASMEDC, 2003. http://dx.doi.org/10.1115/fbc2003-169.

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Petroleum coke is regarded as a difficult fuel because of its high sulphur content and low volatile content. However, its low price and increased production, means that there is a powerful economic stimulus to use it for power generation. In this work, a process simulation has been performed as part of a feasibility study on the utilization of petroleum coke for power generation with low-cost CO2 capture. The proposed system employs a pressurized fluidized bed combustor and a calciner. In the combustor itself, the petroleum coke is burned and most of the CO2 generated is captured by a CaO sorbent under pressurized condition to form CaCO3. The CaCO3 is transported into the calciner where limited proportion of the petroleum coke is burned with pure O2, and calcines the spent sorbent back into CaO and CO2. A nearly pure CO2 stream is obtained from the calciner for subsequent disposal or utilization. The predicted overall efficiency of the combustion is near 40%. The proposed system would also be suitable for firing other high carbon and low ash fuel, such as anthracite.
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Brandauer, M., A. Schulz, and S. Wittig. "Mechanisms of Coke Formation in Gas Turbine Combustion Chambers." In ASME 1995 International Gas Turbine and Aeroengine Congress and Exposition. American Society of Mechanical Engineers, 1995. http://dx.doi.org/10.1115/95-gt-049.

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New gas turbine combustor designs are developed to reduce pollutant and NOx-emissions. In these new combustors, the formation of carbonaceous deposits, especially in prevaporizers, affects the reliablility and effectiveness of operation. To avoid deposits, a detailed knowledge of the origins and mechanisms of formation is required. To obtain a deeper insight, the phenomena were studied systematically. The deposits under consideration show differing characteristics suggesting more than one formation mechanism in the combustor. Consequently, the primary goal was to identify the formation mechanisms and, subsequently, to simulate the mechanisms under well-defined conditions in bench tests for determining the relevant parameters of deposit build-up. The mechanisms of formation were identified based on the properties of the deposits in the combustion chamber. In order to characterize the deposits, physical and chemical analysis techniques were utilized. In summary, tests and numerical predictions identified two major paths of formation: a deposit build-up resulting from flame products such as soot or coked droplets and a deposit build-up resulting from liquid fuel impinging the wall accompanied with chemical reactions at the wall. The deposits caused by fuel droplet impingement were intensively studied in bench tests. In analyzing the processes, the influence of wall temperature, fuel composition, and the oxygen content in the environment is shown in detail. In addition, the importance of thermal instabilities of the fuel, previously studied under fuel supply system conditions, is demonstrated for a deposit formation inside a combustion chamber.
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Anthony, E. J., L. Jia, and S. M. Burwell. "Petroleum Coke FBC Ash: A Detailed Look at Calcium in the Ash." In 17th International Conference on Fluidized Bed Combustion. ASMEDC, 2003. http://dx.doi.org/10.1115/fbc2003-172.

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Petroleum coke combustion is different from coal and its behaviour in an FBC environment clearly illustrates this. Analysis of bed ash from the CFBC boilers owned and operated by the Nelson Industrial Steam Company Ltd. (NISCO) was examined in detail to determine the fate of calcium in the ash using a range of techniques. These analyses have shown a free lime content, which is significantly lower than expected based on the elemental analysis of the bed material. Using different methods of analyses than have been typically used for FBC ashes (coal in particular) it would appear that between 6 to 7% of the total CaO in the samples is combined in the form of acid soluble and insoluble other calcium compounds (OCC). This translates to about 30% less free lime (depending on the ash sulfur content) in the sample than would be calculated based on a standard chemical analysis of the bed ash. This current work has identified about 1% of the missing CaO in the form of acid insoluble Ca and Mg vanadates with perhaps as much as 2% of the remaining missing CaO present as soluble OCC.
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Iribarne, J. V., E. J. Anthony, and A. Iribarne. "A Scanning Electron Microscope Study on Agglomeration in Petroleum Coke-Fired FBC Boiler." In 17th International Conference on Fluidized Bed Combustion. ASMEDC, 2003. http://dx.doi.org/10.1115/fbc2003-082.

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Ten samples, from different FBC boiler systems burning petroleum coke, were chosen to study the development, structure and composition of deposits formed by agglomeration at various locations in the boilers. The work focused on examination of the samples by scanning electron microscopy (SEM) and dispersive X-ray analysis (EDX). Chemical analysis and other techniques were also employed. The results obtained have not brought to light any evidence of the participation of the liquid phase or of vanadium or alkaline metal compounds. The CaSO4 of the deposits is high (80 to 100%) and the agglomeration results from the prolonged sintering of CaSO4 particles, until a strong 3-dimensional framework is formed, in which other, unrelated particles may be trapped, without contributing to cohesion. While CaO is still available, “chemical sintering” associated with its conversion to CaSO4 appears to be important, but sintering also occurs by a slower mass transfer mechanism and continues after the depletion of CaO. Deposits formed in regions only reached by fly ash (convection section), and also in-bed deposits, grow from particles <50 μm, mostly very small ones, < 10 μm. Where the bed ash can collect (e.g., J-valves), the deposits grow by the sintering together of larger particles, 100–300 μm, which themselves appear to be conglomerates of smaller particles sintered together.
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Zhang, Chun-Lin, De-Chang Liu, and Han-Ping Chen. "The Effects of Heterogeneous Reactions on the Reduction of NO in Petroleum-Coke-Fired Fluidized Beds." In 18th International Conference on Fluidized Bed Combustion. ASMEDC, 2005. http://dx.doi.org/10.1115/fbc2005-78085.

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Because of high heating value, low volatile, high nitrogen content and high sulfur content, some kinds of petroleum coke are only suitable for use as fuel, especially combusted in fluidized beds. Based on experiments in a 1t/h fluidized bed, we found that lots of NO and N2O were emitted, and they reached to 780ppm and 150ppm respectively. By analyzing the contributions of char-N and volatile-N to the formation of NO and N2O, we also found it was more important to control the combustion of char to reduce the emission of NO and N2O. This paper tried to find a denitrification agent that could work as desulfuration agent in fluidized beds. We chose Fe as the denitrification agent. The influence of iron on the reduction of NO was studied on. The effects of petroleum-coke char, CO and limestone on the reaction of iron and NO were investigated in a bench scale fluidized bed. Quantitative Fe and petroleum coke char were added into a quartz sand bed respectively, the conversions of NO between these conditions were compared with. The results showed that the ability of Fe to reduce NO was much stronger than the char, and the conversion of NO almost reached to 100%. After minutes that depended on the amount of Fe, Fe was oxidized to oxide of Fe, and the conversion of NO decreased. Petroleum coke char could deoxidize the oxide of Fe. Fe that mixed with petroleum coke char could apparently increase the reaction time of Fe and NO. CO was also a reductive agent of the oxide of Fe, but the effect was not strong as char. Limestone little increased the conversion of NO. From the experiments, we suggested that iron or its oxides would be a possible denitrification agent to reduce NO in fluidized beds in situ.
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Reports on the topic "Coke – Combustion"

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Anthony, E. J., H. A. Becker, R. K. Code, R. W. McCleave, and J R Stephenson. Bubbling fluidized bed combustion of Syncrude coke. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1987. http://dx.doi.org/10.4095/304362.

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Anthony, E. J., and F. D. Friedrich. Fluidized bed combustion of petroleum coke at CANMET. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1986. http://dx.doi.org/10.4095/302644.

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Wong, J. K., G. N. Banks, and H. Whaley. Pilot-scale combustion performance tests on Obed clean coal/petroleum coke blends. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1994. http://dx.doi.org/10.4095/304610.

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Anthony, E. J., D. L. Desai, and F. D. Friedrich. Combustion trials with syncrude coke in a pilotscale atmospheric bubbling fluidized bed. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1986. http://dx.doi.org/10.4095/302662.

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Banks, G. N., J. K. L. Wong, and H. Whaley. Combustion data for petroleum coke and waste fuel oil for Les Sables OLIMAG Inc. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1992. http://dx.doi.org/10.4095/304530.

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Caswell, Andrew W. High Impact Technology Compact Combustion (HITCC) Compact Core Technologies. Fort Belvoir, VA: Defense Technical Information Center, January 2016. http://dx.doi.org/10.21236/ad1003182.

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Rohatgi, Upendra, and Michael Furey. Commercialization of Turbulent Combustion Code CREBCOM for Chemical Industry Safety. Office of Scientific and Technical Information (OSTI), June 2007. http://dx.doi.org/10.2172/973829.

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Kellar, S. A., W. R. A. Huff, E. J. Moler, S. Yeah, and Z. Hussain. Characterization of combustion chamber products by core-level photoabsorption spectroscopy. Office of Scientific and Technical Information (OSTI), April 1997. http://dx.doi.org/10.2172/603652.

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Grcar, Joseph F. An Explicit Runge-Kutta Iteration for Diffusion in the Low MachNumber Combustion Code. Office of Scientific and Technical Information (OSTI), August 2007. http://dx.doi.org/10.2172/927034.

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Kuwabara, Fumio, Kuniki Kanayama, Hiroki Arai, Jin Kusaka, Tomoyuki Wakisaka, and Yasuhiro Daisho. Numerical Analysis of Diesel Combustion by GIT Code Account for Detailed Chemical Reactions. Warrendale, PA: SAE International, May 2005. http://dx.doi.org/10.4271/2005-08-0316.

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