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Thermodynamic analysis of aqueous phase reforming of three model compounds in bio-oil for hydrogen production
Xie, Jianjun1; Su, Deren1; Yin, Xiuli1; Wu, Chuangzhi1; Zhu, Jingxu2
2011-12-01
发表期刊INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
卷号36期号:24页码:15561-15572
摘要Thermodynamic analysis with Gibbs free energy minimization was performed for aqueous phase reforming of methanol, acetic acid, and ethylene glycol as model compounds for hydrogen production from bio-oil. The effects of the temperature (340-660 K) and pressure ratio P-sys/P-H2O (0.1-2.0) on the selectivity of H-2 and CH4, formation of solid carbon, and conversion of model compounds were analyzed. The influences of CaO and O-2 addition on the formation of H-2, CH4, and CO2 in the gas phase and solid phase carbon, CaCO3, and Ca(OH)(2) were also investigated. With methanation and carbon formation, the conversion of the model compounds was >99.99% with no carbon formation, and methanation was thermodynamically favored over hydrogen production. H-2 selectivity was greatly improved when methanation was suppressed, but most of the inlet model compounds formed solid carbon. After suppressing both methanation and carbon formation, aqueous phase reforming of methanol, acetic acid and ethylene glycol at 500 K and with P-sys/P-H2O = 1.1 gave H-2 selectivity of 74.98%, 66.64% and 71.38%, respectively. These were similar to the maximum stoichiometric hydrogen selectivity of 75.00% (methanol), 66.67% (acetic acid), and 71.43% (ethylene glycol). At 500 K and 2.90 MPa, as the molar ratio of CaO/BMCs increased, the normalized variation in H-2 increased and that for CH4 decreased. Formation of solid carbon was effectively suppressed by addition of O-2, but this was at the expense of H-2 formation. With the O-2/BMCs molar ratio regulated at 1.0, oxidation and CO2 capture increased the normalized variation in H-2 to 33.33% (methanol), 50.00% (acetic acid), and 60.00% (ethylene glycol), and the formation of solid carbon decreased to zero. Copyright (C) 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
文章类型Article
关键词Bio-oil Aqueous Phase Reforming Hydrogen Production Thermodynamic Analysis Sorption Enhanced Oxidation
WOS标题词Science & Technology ; Physical Sciences ; Technology
DOI10.1016/j.ijhydene.2011.08.103
研究领域[WOS]Chemistry ; Electrochemistry ; Energy & Fuels
关键词[WOS]ETHYLENE-GLYCOL ; DIMETHYL ETHER ; FUEL-CELLS ; STEAM ; GLYCEROL ; BIOMASS ; HYDROCARBONS ; GENERATION ; ADSORPTION ; CATALYSTS
收录类别SCI
语种英语
WOS类目Chemistry, Physical ; Electrochemistry ; Energy & Fuels
WOS记录号WOS:000297089700009
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被引频次:37[WOS]   [WOS记录]     [WOS相关记录]
文献类型期刊论文
条目标识符http://ir.giec.ac.cn/handle/344007/10372
专题中国科学院广州能源研究所
作者单位1.Chinese Acad Sci, Guangzhou Inst Energy Convers, Key Lab Renewable Energy & Gas Hydrate, Guangzhou 510640, Peoples R China
2.Univ Western Ontario, Dept Chem Engn, London, ON N6A 5B9, Canada
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Xie, Jianjun,Su, Deren,Yin, Xiuli,et al. Thermodynamic analysis of aqueous phase reforming of three model compounds in bio-oil for hydrogen production[J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY,2011,36(24):15561-15572.
APA Xie, Jianjun,Su, Deren,Yin, Xiuli,Wu, Chuangzhi,&Zhu, Jingxu.(2011).Thermodynamic analysis of aqueous phase reforming of three model compounds in bio-oil for hydrogen production.INTERNATIONAL JOURNAL OF HYDROGEN ENERGY,36(24),15561-15572.
MLA Xie, Jianjun,et al."Thermodynamic analysis of aqueous phase reforming of three model compounds in bio-oil for hydrogen production".INTERNATIONAL JOURNAL OF HYDROGEN ENERGY 36.24(2011):15561-15572.
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