Modeling for a Catalytic Plate Reactor Coupling Endothermic Methanol Steam Reforming and Hydrogen Combustion
碩士 === 大同大學 === 化學工程學系(所) === 99 === In this work, tubular and plate reactors for carrying out methanol steam reforming reactions are simulated using Fluent software. The simulation results using Fluent software are confirmed by the performance of an isothermal plug flow tubular reactor in which the...
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ndltd-TW-099TTU050630302015-10-13T20:27:49Z http://ndltd.ncl.edu.tw/handle/19247797344395818304 Modeling for a Catalytic Plate Reactor Coupling Endothermic Methanol Steam Reforming and Hydrogen Combustion 結合吸熱之甲醇重組反應與氫氣燃燒之平板催化反應器之模擬 Chang-Che Liu 劉昌哲 碩士 大同大學 化學工程學系(所) 99 In this work, tubular and plate reactors for carrying out methanol steam reforming reactions are simulated using Fluent software. The simulation results using Fluent software are confirmed by the performance of an isothermal plug flow tubular reactor in which the methanol steam reforming reactions are performed. Among the eight different reactor designs, the catalytic plate reactor packed with small catalyst particles coupling endothermic methanol steam reforming and hydrogen combustion system give the best performance. The conversion of methanol is 0.63 for the isothermal (250℃) plug flow tubular reactor while that for the catalytic plate reactor packed with small catalyst particles coupling endothermic methanol steam reforming and hydrogen combustion system is 0.6 if the mass transfer resistance between the gas reactants and the catalyst particles is not included in the simulation using Fluent software. Jyh-Shyong Chang 張志雄 2011 學位論文 ; thesis 99 zh-TW |
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碩士 === 大同大學 === 化學工程學系(所) === 99 === In this work, tubular and plate reactors for carrying out methanol steam reforming reactions are simulated using Fluent software. The simulation results using Fluent software are confirmed by the performance of an isothermal plug flow tubular reactor in which the methanol steam reforming reactions are performed. Among the eight different reactor designs, the catalytic plate reactor packed with small catalyst particles coupling endothermic methanol steam reforming and hydrogen combustion system give the best performance. The conversion of methanol is 0.63 for the isothermal (250℃) plug flow tubular reactor while that for the catalytic plate reactor packed with small catalyst particles coupling endothermic methanol steam reforming and hydrogen combustion system is 0.6 if the mass transfer resistance between the gas reactants and the catalyst particles is not included in the simulation using Fluent software.
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Jyh-Shyong Chang |
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Jyh-Shyong Chang Chang-Che Liu 劉昌哲 |
author |
Chang-Che Liu 劉昌哲 |
spellingShingle |
Chang-Che Liu 劉昌哲 Modeling for a Catalytic Plate Reactor Coupling Endothermic Methanol Steam Reforming and Hydrogen Combustion |
author_sort |
Chang-Che Liu |
title |
Modeling for a Catalytic Plate Reactor Coupling Endothermic Methanol Steam Reforming and Hydrogen Combustion |
title_short |
Modeling for a Catalytic Plate Reactor Coupling Endothermic Methanol Steam Reforming and Hydrogen Combustion |
title_full |
Modeling for a Catalytic Plate Reactor Coupling Endothermic Methanol Steam Reforming and Hydrogen Combustion |
title_fullStr |
Modeling for a Catalytic Plate Reactor Coupling Endothermic Methanol Steam Reforming and Hydrogen Combustion |
title_full_unstemmed |
Modeling for a Catalytic Plate Reactor Coupling Endothermic Methanol Steam Reforming and Hydrogen Combustion |
title_sort |
modeling for a catalytic plate reactor coupling endothermic methanol steam reforming and hydrogen combustion |
publishDate |
2011 |
url |
http://ndltd.ncl.edu.tw/handle/19247797344395818304 |
work_keys_str_mv |
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