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    Thermodynamic Analysis on Reaction Characteristics of the Coupling Steam, CO2 and O2 Reforming of Methane

    Source: Journal of Energy Resources Technology:;2018:;volume 140:;issue 010::page 102203
    Author:
    Yan, Yunfei
    ,
    Yan, Hongyu
    ,
    Li, Lixian
    ,
    Zhang, Li
    ,
    Yang, Zhongqing
    DOI: 10.1115/1.4040074
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: This study presents an analysis of coupling steam, CO2 and O2 reforming of CH4 using the thermodynamic equilibrium constant method. Effects of molar ratio of O2/CH4, H2O/CH4 and CO2/CH4 on reforming characteristics in both carbon deposition and carbon-free systems are analyzed. The results indicate that CH4 conversion rate, H2, and CO yield increase with increasing O2/CH4 molar ratio in two systems. In addition, the carbon elimination is achieved when O2/CH4 ratio increases to 0.31, and changing the amount of O2 can be an effective way to alter n(H2)/n(CO) ratio in the carbon deposition systems. CH4 conversion rate increases with increasing H2O/CH4 ratio in the carbon-free system, while it declines in the carbon deposition system. H2O plays a role of altering n(H2)/n(CO) ratio, and its effects on two systems are opposite. The deposited carbon is totally eliminated when H2O/CH4 ratio increases to 0.645. The increase of CO2/CH4 molar ratio leads to a rapid increase of CO2 conversion when CO2/CH4 ratio is less than 0.5. A slightly change of CO2/CH4 ratio can result in a huge difference on n(H2)/n(CO) ratio in both systems, and carbon elimination is achieved at CO2/CH4 = 0.99. The analyzed results have theoretical significance to efficiently catalyze methane coupling.
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      Thermodynamic Analysis on Reaction Characteristics of the Coupling Steam, CO2 and O2 Reforming of Methane

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    contributor authorYan, Yunfei
    contributor authorYan, Hongyu
    contributor authorLi, Lixian
    contributor authorZhang, Li
    contributor authorYang, Zhongqing
    date accessioned2019-02-28T10:56:27Z
    date available2019-02-28T10:56:27Z
    date copyright5/15/2018 12:00:00 AM
    date issued2018
    identifier issn0195-0738
    identifier otherjert_140_10_102203.pdf
    identifier urihttp://yetl.yabesh.ir/yetl1/handle/yetl/4251003
    description abstractThis study presents an analysis of coupling steam, CO2 and O2 reforming of CH4 using the thermodynamic equilibrium constant method. Effects of molar ratio of O2/CH4, H2O/CH4 and CO2/CH4 on reforming characteristics in both carbon deposition and carbon-free systems are analyzed. The results indicate that CH4 conversion rate, H2, and CO yield increase with increasing O2/CH4 molar ratio in two systems. In addition, the carbon elimination is achieved when O2/CH4 ratio increases to 0.31, and changing the amount of O2 can be an effective way to alter n(H2)/n(CO) ratio in the carbon deposition systems. CH4 conversion rate increases with increasing H2O/CH4 ratio in the carbon-free system, while it declines in the carbon deposition system. H2O plays a role of altering n(H2)/n(CO) ratio, and its effects on two systems are opposite. The deposited carbon is totally eliminated when H2O/CH4 ratio increases to 0.645. The increase of CO2/CH4 molar ratio leads to a rapid increase of CO2 conversion when CO2/CH4 ratio is less than 0.5. A slightly change of CO2/CH4 ratio can result in a huge difference on n(H2)/n(CO) ratio in both systems, and carbon elimination is achieved at CO2/CH4 = 0.99. The analyzed results have theoretical significance to efficiently catalyze methane coupling.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleThermodynamic Analysis on Reaction Characteristics of the Coupling Steam, CO2 and O2 Reforming of Methane
    typeJournal Paper
    journal volume140
    journal issue10
    journal titleJournal of Energy Resources Technology
    identifier doi10.1115/1.4040074
    journal fristpage102203
    journal lastpage102203-8
    treeJournal of Energy Resources Technology:;2018:;volume 140:;issue 010
    contenttypeFulltext
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    DSpace software copyright © 2002-2015  DuraSpace
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