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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
Source PublicationINTERNATIONAL JOURNAL OF HYDROGEN ENERGY
Volume36Issue:24Pages:15561-15572
AbstractThermodynamic 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.
SubtypeArticle
KeywordBio-oil Aqueous Phase Reforming Hydrogen Production Thermodynamic Analysis Sorption Enhanced Oxidation
WOS HeadingsScience & Technology ; Physical Sciences ; Technology
DOI10.1016/j.ijhydene.2011.08.103
WOS Subject ExtendedChemistry ; Electrochemistry ; Energy & Fuels
WOS KeywordETHYLENE-GLYCOL ; DIMETHYL ETHER ; FUEL-CELLS ; STEAM ; GLYCEROL ; BIOMASS ; HYDROCARBONS ; GENERATION ; ADSORPTION ; CATALYSTS
Indexed BySCI
Language英语
WOS SubjectChemistry, Physical ; Electrochemistry ; Energy & Fuels
WOS IDWOS:000297089700009
Citation statistics
Cited Times:37[WOS]   [WOS Record]     [Related Records in WOS]
Document Type期刊论文
Identifierhttp://ir.giec.ac.cn/handle/344007/10372
Collection中国科学院广州能源研究所
Affiliation1.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
Recommended Citation
GB/T 7714
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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