Relevant bibliographies by topics / Gasification reactor

Contents

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

Academic literature on the topic 'Gasification reactor'

Author: Grafiati
Published: 4 June 2021
Last updated: 14 February 2022

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Journal articles on the topic "Gasification reactor"

1

Nyoman Suprapta Winaya, I., I. Ketut Gede Wirawan, I. Wayan Arya Darma, I. Putu Lokantara, and Rukmi Sari Hartati. "An increase in bed temperature on gasification of dual reactor fluidized bed." E3S Web of Conferences 67 (2018): 02059. http://dx.doi.org/10.1051/e3sconf/20186702059.

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One of the main issues using biomass as fuel in air gasification is the dilution of its product gas by the nitrogen in the air. A dual reactor fluidized bed (DRFB) overcomes this problem in which the gasification and combustion reactions are decoupled and conducted in two separate fluidized bed reactors connected by circulating bed material. The DFRB unit made of 304 stainless steel pipe with a height of 100 and 150 cm, and inner diameters (i.d.) of 15.2 and 5.1 cm for gasifier and combustor respectively. The rice husk as fuel and quartz sand as bed material having the same size of 0.4 - 0.6 m
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Zarzycki, Robert. "Pulverized coal gasification with steam and flue gas." MATEC Web of Conferences 240 (2018): 05036. http://dx.doi.org/10.1051/matecconf/201824005036.

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The study presents the concept and numerical calculations of the coal dust gasification in the entrained flow reactor with power of 16 MWt. The gasification process in the reactor can be performed in the atmosphere of O2, CO2 and H2O. The combustible gases obtained during gasification are composed mainly of CO and H2 and can be used to feed pulverized coal-fired boilers. Integration of the reactor (reactors) for coal dust gasification with the pulverized coal-fired boiler allows for improved flexibility, especially in the range of low loads if stabilization of coal dust combustion in pulverize
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Zhao, Li Hong, Xi Jie Chu, and Shao Juan Cheng. "Kinetic Study of CO2 Gasification of Coal Chars." Advanced Materials Research 550-553 (July 2012): 2754–57. http://dx.doi.org/10.4028/www.scientific.net/amr.550-553.2754.

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The CO2 gasification of three coal chars were investigated for determining the gasification reactivity and the kinetic parameters. Experiments were conducted in a fluidized-bed reactor at temperature of 1173 k, 1273 k and 1373 k at atmospheric pressure. Gasification kinetic parameters of the samples were determined using Homogeneous model and shrinking-core model. It is found that the gasification reaction under chemical-reaction-rate control, the gasification reactivity of coal char are strongly dependent on the rank of coals and gasification temperature. Both models could describe CO2 gasifi
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Tokmurzin, D., and D. Adair. "Development of Euler-Lagrangian Simulation of a Circulating Fluidized Bed Reactor for Coal Gasification." Eurasian Chemico-Technological Journal, no. 1 (February 20, 2019): 45. http://dx.doi.org/10.18321/ectj789.

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A Computational Particle Fluid Dynamics (CPFD) model based on the Multiphase Particle in Cell (MP-PIC) approach is used for Shubarkol coal gasification simulation in an atmospheric circulating fluidized bed reactor. The simulation is developed on a basis of experimental data available from a biomass gasification process. The cross-section diameter of the reactor riser is 200 mm and the height is 6500 mm. The Euler-Lagrangian simulation is validated using experimental data available in the literature and also compared with an Euler-Euler simulation. The gasification reactions kinetics model is
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Mularski, Jakub, and Norbert Modliński. "Impact of Chemistry–Turbulence Interaction Modeling Approach on the CFD Simulations of Entrained Flow Coal Gasification." Energies 13, no. 23 (2020): 6467. http://dx.doi.org/10.3390/en13236467.

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This paper examines the impact of different chemistry–turbulence interaction approaches on the accuracy of simulations of coal gasification in entrained flow reactors. Infinitely fast chemistry is compared with the eddy dissipation concept considering the influence of turbulence on chemical reactions. Additionally, ideal plug flow reactor study and perfectly stirred reactor study are carried out to estimate the accuracy of chosen simplified chemical kinetic schemes in comparison with two detailed mechanisms. The most accurate global approach and the detailed one are further implemented in the
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Li, Liu Yun, Hiroo Kunii, Masamitsu Yamauchi, Hee Joon Kim, and Tadaaki Shimizu. "Steam Gasification for Biomass Tar with Natural Ores of Limonite and Dolomite." Advanced Materials Research 608-609 (December 2012): 201–5. http://dx.doi.org/10.4028/www.scientific.net/amr.608-609.201.

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Light gases were produced from biomass tar gasification using limonite and dolomite as catalysts. Experiments were performed in a fixed bed reactor with the gasification temperatures of 600–800 °C. Limonite gave the obvious effect on the tar gasification, and the light gases of hydrogen and carbon oxides were mainly obtained. Also, the gas yields depended on the catalytic temperature. Hydrogen yields tend to increasing with temperatures from 650 to 800 °C. The reaction equilibrium was changed by dolomite addition in the reactor system; hydrogen gas was doubled with the limonite and dolomite mi
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Dolu, Cem, and Lutfullah Kuddusi. "The effect of reactor height on coal gasification." Thermal Science 21, no. 5 (2017): 1937–51. http://dx.doi.org/10.2298/tsci150526112d.

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A comprehensive 2-D numerical model has been developed to simulate the coal gasification and investigate the effect of reactor height on the coal gasification in fluidized bed. Gas-solid flow, homogeneous and heterogeneous chemical reactions were considered. An Eulerian model for fluid phase and discrete particle method (Lagrangian) for particle phase were used in this study. The reaction rates of homogeneous and heterogeneous reactions were determined by Arrhenius-eddy dissipation reaction rate and Arrhenius-diffusion rate, respectively. Simulations were performed in a fluidized bed coal gasi
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Nguyen, Nhut M., Falah Alobaid, and Bernd Epple. "Process Simulation of Steam Gasification of Torrefied Woodchips in a Bubbling Fluidized Bed Reactor Using Aspen Plus." Applied Sciences 11, no. 6 (2021): 2877. http://dx.doi.org/10.3390/app11062877.

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A comprehensive process model is proposed to simulate the steam gasification of biomass in a bubbling fluidized bed reactor using the Aspen Plus simulator. The reactor models are implemented using external FORTRAN codes for hydrodynamic and reaction kinetic calculations. Governing hydrodynamic equations and kinetic reaction rates for char gasification and water-gas shift reactions are obtained from experimental investigations and the literature. Experimental results at different operating conditions from steam gasification of torrefied biomass in a pilot-scale gasifier are used to validate the
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Abdelrahman, Ameen, Hassan A. Dosky, Hamdy F. M. Mohamed, Aly M. Radwan, and Asmaa S. Hamouda. "Studying and Evaluating Sustainable Materials for Converting Plastic Waste to Fuel." Energy and Environment Research 8, no. 1 (2018): 73. http://dx.doi.org/10.5539/eer.v8n1p73.

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Gasification is one of the most important solutions for plastic waste management. We researched the conversion of plastic waste to fuel using sustainable material (Nano Clay) modified with Nano transition metals (TiO2, MnO, and ZnO). This was processed in a fix bed reactor design. After studying the reaction mechanism of the gasification process, we evaluated the optimize (reactor temperature, reaction time and feeding ratio of the modified catalyst) on the gasification process with its application for the modified catalyst on the degradation of polyethylene high density(PEHD), other waste pla
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Ahmed, Reem, Chandra Mohan Sinnathambi, and Usama Eldmerdash. "Dynamic Studies of Refinery Sludge Gasification in Updraft Reactor." Applied Mechanics and Materials 625 (September 2014): 431–34. http://dx.doi.org/10.4028/www.scientific.net/amm.625.431.

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Many papers have been published about the gasification of different biomass fuels in fixed bed reactor. To date, no experimental analysis is available in the open literature on gasification of refinery sludge. Therefore the descriptions of dynamic temperature in an updraft reactor for a dry refinery sludge gasification are investigated in details. The rate of the temperature change with operation time and the temperature profiles inside the reactor are taken for various equivalent ratios. The dynamic results show that increasing the ER from 0.195 to 0.244 shift the combustion zone peak tempera
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Dissertations / Theses on the topic "Gasification reactor"

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Earp, David M. "Gasification of biomass in a downdraft reactor." Thesis, Aston University, 1988. http://publications.aston.ac.uk/10218/.

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The objective of this study was to design, construct, commission and operate a laboratory scale gasifier system that could be used to investigate the parameters that influence the gasification process. The gasifier is of the open-core variety and is fabricated from 7.5 cm bore quartz glass tubing. Gas cleaning is by a centrifugal contacting scrubber, with the product gas being flared. The system employs an on-line dedicated gas analysis system, monitoring the levels of H2, CO, CO2 and CH4 in the product gas. The gas composition data, as well as the gas flowrate, temperatures throughout the sys
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Mansaray, Kelleh Gbawuru. "Gasification of rice husk in a fluidized bed reactor." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1998. http://www.collectionscanada.ca/obj/s4/f2/dsk2/tape17/PQDD_0022/NQ31530.pdf.

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Z'Graggen, Andreas. "Solar gasification of carbonaceous materials : reactor design, modeling and experimentation /." kostenfrei, 2008. http://e-collection.ethbib.ethz.ch/view/eth:30596.

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Hägglund, Philip. "Commissioning of Entrained Flow Reactor for Combustion and Gasification Research." Thesis, Luleå tekniska universitet, Institutionen för teknikvetenskap och matematik, 2017. http://urn.kb.se/resolve?urn=urn:nbn:se:ltu:diva-66204.

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Rasol, Hepa. "Influence of Potassium on Gasification Performance." Thesis, Högskolan i Borås, Akademin för textil, teknik och ekonomi, 2016. http://urn.kb.se/resolve?urn=urn:nbn:se:hb:diva-10350.

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To release energy from chemically stored energy in the biomass was the new investigation in recent years. Utilizing of biomass for this purpose occur in two different ways, directly by burning (combustion) the biomass and indirectly by pyrolysis process which will convert the biomass to three main products, bio- tar, bio- char and synthetic gas. Biomass contains different amount of inorganic compound, especially alkali metals which causes some diverse impacts on combustion, pyrolysis and gasification process such as corrosion, agglomeration and fouling problems. This project aims to investigat
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McKinnon, Hamish Alexander. "Improved Hydrogen Production from Biomass Gasification in a Dual Fluidissed Bed Reactor." Thesis, University of Canterbury. Chemical and Process Engineering, 2009. http://hdl.handle.net/10092/4459.

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Biomass gasification is a technology under development that presents a means of generating hydrogen using renewable energy. While many forms of gasification have been investigated, steam gasification using a dual fluidised bed (DFB) reactor has been shown to efficiently produce high hydrogen content producer gas. The aims of this research were to increase the hydrogen yield from the 100kW DFB gasifier installed at the University of Canterbury, and thereby improve the current state of the art of gasifier operation. Calcium carbonate-based minerals such as calcite and dolomite were shown to be
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Al-Hwayzee, Mohammed. "Design and development of gasification processes in fluidised bed chemical reactor engineering." Thesis, Cardiff University, 2016. http://orca.cf.ac.uk/97762/.

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This thesis focuses on studying and investigation the effects of the hydrodynamic and operating parameters in the air-biomass gasification in a bubbling fluidised bed gasifier under low temperature (< 800°C) conditions and evaluating the potential of the gasification of two solid biomass waste materials, Iraqi date palm wastes and sawdust pinewood. These parameters are air flowrate, particle size of the sand bed material, biomass particle size, static bed height, air equivalence ratio, bed temperature, number of holes in distributor plates and biomass fuel type. A design study was conducted to
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Hassan, Mohamed. "Modelling and simulation of biomass gasification in a circulating fluidized bed reactor." Thesis, Aston University, 2013. http://publications.aston.ac.uk/20858/.

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Computational Fluid Dynamics (CFD) has found great acceptance among the engineering community as a tool for research and design of processes that are practically difficult or expensive to study experimentally. One of these processes is the biomass gasification in a Circulating Fluidized Bed (CFB). Biomass gasification is the thermo-chemical conversion of biomass at a high temperature and a controlled oxygen amount into fuel gas, also sometime referred to as syngas. Circulating fluidized bed is a type of reactor in which it is possible to maintain a stable and continuous circulation of solids i
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PHOUNGLAMCHEIK, Aekjuthon. "Modellering av pyrolys i roterande trumma." Thesis, KTH, Skolan för kemivetenskap (CHE), 2015. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-173840.

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This project focuses on the numerical modeling of a rotary kiln pyrolyzer such as found in the e.g. WoodRoll multistage gasification process. The model consists of two parts: a granular flow model, and a pyrolyzer model. In the first part, Saeman's equation was employed to develop a model which can describe the behavior of solid granular flow in a rotary kiln without reaction. Residence-time distribution (RTD) is the main aim to study in this part, which was simulated by axial dispersion model (ADM). The model requires only one fitting parameter that is dispersion coefficient (Dax), which was
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Hlebak, Joshua J. "Equilibrium Modeling, Design, Construction, and Validation Testing of a Pilot Scale, USS Gasification Reactor." Ohio University / OhioLINK, 2011. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1314293669.

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Books on the topic "Gasification reactor"

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Earp, David Martyn. Gasification of biomass in a downdraft reactor. Aston University. Department of Chemical Engineering., 1988.

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Gokhale, Ashokkumar J. Devolatilization studies on coals in a fixed bed reactor. 1985.

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Collins, John Patrick. Catalytic decomposition of ammonia in a membrane reactor. 1993.

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Aarsen, F. G. van den. and Commission of the European Communities. Directorate-General for Science, Research and Development., eds. Energy recovery by gasification of agricultural and forestry wastes in fluidized bed reactors and in moving bed reactors with internalrecycle of pyrolysis gas: Process development and reactor modelling. Commission of the European Communities, 1986.

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Aarsen, F. G. van den. and Commission of the European Communities. Directorate-General for Science, Research and Development., eds. Energy recovery by gasification of agricultural and forestry wastes in fluidized bed reactors and in moving bed reactors with internal recycle of pyrolysis gas: Process development and reactor modelling. Commission of the European Communities, 1986.

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(Canada), Bioenergy Development Program, ed. Economic feasibility of wood gasification using a plasma pyrolysis reactor =: La faisabilité économique de la gazéification du bois à l'aide d'un réacteur de pyrolyse utilisant du plasma. Pulp and Paper Research Institute of Canada, 1985.

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Book chapters on the topic "Gasification reactor"

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Li, Qiang, and Jiansheng Zhang. "COAL GASIFICATION." In Multiphase Reactor Engineering for Clean and Low-Carbon Energy Applications. John Wiley & Sons, Inc., 2017. http://dx.doi.org/10.1002/9781119251101.ch3.

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Agarwal, Ramesh K., Mengqiao Yang, and Subhodeep Banerjee. "Transient Cold Flow Simulation of a Fast Fluidized Bed Fuel Reactor for Chemical Looping Combustion." In Coal and Biomass Gasification. Springer Singapore, 2017. http://dx.doi.org/10.1007/978-981-10-7335-9_13.

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Walawender, Walter P., Deborah A. Hoveland, and L. T. Fan. "Steam Gasification of Aplha Cellulose in a Fluid Bed Reactor." In Fundamentals of Thermochemical Biomass Conversion. Springer Netherlands, 1985. http://dx.doi.org/10.1007/978-94-009-4932-4_49.

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Hallgren, Anders, Lars A. Andersson, and Ingemar Bjerle. "High Temperature Gasification of Biomass in an Atmospheric Entrained Flow Reactor." In Advances in Thermochemical Biomass Conversion. Springer Netherlands, 1993. http://dx.doi.org/10.1007/978-94-011-1336-6_26.

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Chamberland, André, and Raynald Labrecque. "Parametric Study of an Oxygen-Blown Fluidised-Bed Reactor for Wood Gasification." In Research in Thermochemical Biomass Conversion. Springer Netherlands, 1988. http://dx.doi.org/10.1007/978-94-009-2737-7_86.

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Szałatkiewicz, Jakub, Grzegorz Zielono, Łukasz Obrzut, and Marzena Szałatkiewicz. "Method of Control for Gasification Reactor in Ecological Technology of Biomass Waste Utilization." In Recent Advances in Systems, Control and Information Technology. Springer International Publishing, 2016. http://dx.doi.org/10.1007/978-3-319-48923-0_31.

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Kaewluan, Sommas, Janewit Wannapeera, and Suneerat Pipatmanomai. "Characteristics of Products from Rubber Woodchip Gasification in a Fluidised-Bed Reactor: Effect of Equivalent Ratio." In Challenges of Power Engineering and Environment. Springer Berlin Heidelberg, 2007. http://dx.doi.org/10.1007/978-3-540-76694-0_236.

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Roh, Seon Ah, Sung Real Son, Sang Done Kim, Woon Jae Lee, and Yong Kuk Lee. "Steam Gasification Characteristics of a Pine-Nut Shell in a Thermobalance and a Fluidized Bed Reactor." In Key Engineering Materials. Trans Tech Publications Ltd., 2005. http://dx.doi.org/10.4028/0-87849-958-x.637.

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Zhang, Yaning, Zhongbin Fu, Bingxi Li, Hongtao Li, and Bo Zhang. "Energy and Exergy Evaluation of Product Gas from Coal/Biomass Blend Gasification in a Dual Circulating Fluidized Bed Reactor." In Cleaner Combustion and Sustainable World. Springer Berlin Heidelberg, 2012. http://dx.doi.org/10.1007/978-3-642-30445-3_82.

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Hussain, Maham, Lemma Dendena Tufa, Suzana Yusup, Haslinda Zabiri, and Syed A. Taqvi. "Aspen Plus® Simulation Studies of Steam Gasification in Fluidized Bed Reactor for Hydrogen Production Using Palm Kernel Shell." In Communications in Computer and Information Science. Springer Singapore, 2017. http://dx.doi.org/10.1007/978-981-10-6463-0_54.

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Conference papers on the topic "Gasification reactor"

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Wallin, Mats, Robert Hellgren, Anders Johansson, Lars Chambert, and Ingemar Bjerle. "Pressurized circulating fluid bed gasification reactor." In Intersociety Energy Conversion Engineering Conference. American Institute of Aeronautics and Astronautics, 1994. http://dx.doi.org/10.2514/6.1994-4007.

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THAPA, RAJAN K., RAJAN JAISWAL, and BRITT M. E. MOLDESTAD. "CPFD SIMULATION OF A FIXED BED GASIFICATION REACTOR." In ENERGY PRODUCTION AND MANAGEMENT 2020. WIT Press, 2020. http://dx.doi.org/10.2495/epm200061.

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Krushna N Patil, Raymond L Huhnke, and Danielle D Bellmer. "Gasification of Switchgrass Using a Unique Downdraft Reactor." In 2008 Providence, Rhode Island, June 29 - July 2, 2008. American Society of Agricultural and Biological Engineers, 2008. http://dx.doi.org/10.13031/2013.24970.

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Hathaway, Brandon J., Jane H. Davidson, and David B. Kittelson. "Solar Gasification of Biomass: Kinetics of Pyrolysis and Steam Gasification in Molten Salt." In ASME 2010 International Mechanical Engineering Congress and Exposition. ASMEDC, 2010. http://dx.doi.org/10.1115/imece2010-39829.

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The use of concentrated solar energy for pyrolysis and gasification of biomass is an efficient means for production of hydrogen rich synthesis gas. Utilizing molten alkali-carbonate salts as a reaction and heat transfer media offers enhanced stability and higher reaction rates to these solar processes. To establish the reaction kinetics, experiments were carried out in an electrically heated molten salt reactor. Cellulose or activated charcoal were pyrolyzed or gasified with steam from 1124 K to 1235 K with and without salt. Arrhenius rate expressions are derived from the data supported by a n
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Walt, I. J. v. d., and N. P. Makaringe. "Optimization of a laboratory scale biomass plasma gasification reactor." In 2015 IEEE International Conference on Plasma Sciences (ICOPS). IEEE, 2015. http://dx.doi.org/10.1109/plasma.2015.7179797.

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Abreu, Monique, Carolina Locatelli Vago, Filipe Arthur Firmino Monhol, Carlos Eduardo Silva Abreu, and Luiz Rafael Resende da Silva. "Coconut shell gasification numerical modeling in a downdraft reactor." In 24th ABCM International Congress of Mechanical Engineering. ABCM, 2017. http://dx.doi.org/10.26678/abcm.cobem2017.cob17-0872.

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Sobolewski, A., T. Iluk, and M. Szul. "Gasification of SRF in a GazEla fixed bed reactor." In ENERGY AND SUSTAINABILITY 2014. WIT Press, 2014. http://dx.doi.org/10.2495/esus140711.

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Thapa, R. K. "Heat transfer optimization in a fluidized bed biomass gasification reactor." In HEAT TRANSFER 2014, edited by B. M. Halvorsen. WIT Press, 2014. http://dx.doi.org/10.2495/ht140161.

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Kleiva, K., R. K. Thapa, and B. M. Halvorsen. "Study of a fluidized bed reactor for gasification of biomass." In AFM2012. WIT Press, 2012. http://dx.doi.org/10.2495/afm120221.

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Gunasegarane, G. S. "Modeling hydrodynamics of bubbling fluidized bed reactor for biomass gasification." In NATIONAL CONFERENCE ON ENERGY AND CHEMICALS FROM BIOMASS (NCECB). AIP Publishing, 2020. http://dx.doi.org/10.1063/5.0005816.

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Reports on the topic "Gasification reactor"

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Michael L. Swanson. Advanced High-Temperature, High-Pressure Transport Reactor Gasification. Office of Scientific and Technical Information (OSTI), 2005. http://dx.doi.org/10.2172/896313.

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Michael Swanson and Daniel Laudal. Advanced High-Temperature, High-Pressure Transport Reactor Gasification. Office of Scientific and Technical Information (OSTI), 2008. http://dx.doi.org/10.2172/965112.

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Merriam, N. W., K. P. Thomas, and C. Y. Cha. Mild gasification of Usibelli coal in an inclined fluidized-bed reactor. Office of Scientific and Technical Information (OSTI), 1991. http://dx.doi.org/10.2172/10106405.

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Merriam, N. W., K. P. Thomas, and C. Y. Cha. Mild gasification of Usibelli coal in an inclined fluidized-bed reactor. Office of Scientific and Technical Information (OSTI), 1991. http://dx.doi.org/10.2172/5986762.

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Mei Hong, Richard D. Noble, and John L. Falconer. Highly Selective H2 Separation Zeolite Membranes for Coal Gasification Membrane Reactor Applications. Office of Scientific and Technical Information (OSTI), 2006. http://dx.doi.org/10.2172/908744.

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Mei Hong, Richard Noble, and John Falconer. Highly Selective H2 Separation Zeolite Membranes for Coal Gasification Membrane Reactor Applications. Office of Scientific and Technical Information (OSTI), 2007. http://dx.doi.org/10.2172/956964.

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Mei Hong, Richard D. Noble, and John L. Falconer. HIGHLY SELECTIVE H2 SEPARATION ZEOLITE MEMBRANES FOR COAL GASIFICATION MEMBRANE REACTOR APPLICATIONS. Office of Scientific and Technical Information (OSTI), 2005. http://dx.doi.org/10.2172/876648.

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Mei Hong, Richard D. Noble, and John L. Falconer. HIGHLY SELECTIVE H2 SEPARATION ZEOLITE MEMBRANES FOR COAL GASIFICATION MEMBRANE REACTOR APPLICATIONS. Office of Scientific and Technical Information (OSTI), 2005. http://dx.doi.org/10.2172/861659.

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Celik, I., and M. Chattree. Trend analysis of coal gasification product yields in an entrained flow reactor. Office of Scientific and Technical Information (OSTI), 1989. http://dx.doi.org/10.2172/6991221.

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Sirignano, William A., and David N. Schiller. Energetic Fuel Droplet Gasification with Liquid-Phase Reaction. Defense Technical Information Center, 1997. http://dx.doi.org/10.21236/ada329877.

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