Thermodynamic analysis of aqueous-reforming of polylols for hydrogen generation

被引:36
作者
Luo, Nianjun
Cao, Fahai
Zhao, Xun
Xiao, Tiancun [1 ]
Fang, Dingye
机构
[1] Univ Oxford, Inorgan Chem Lab, Wolfson Catalysis Ctr, Oxford OX1 2JD, England
[2] E China Univ Sci & Technol, Inst Chem Technol, Shanghai 200237, Peoples R China
[3] E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
基金
中国国家自然科学基金;
关键词
polylols reforming; hydrogen generation; thermodynamic calculations;
D O I
10.1016/j.fuel.2006.12.016
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
This paper aims to study the thermodynamic features of polylols reforming to generate hydrogen gas. Polylols can be converted into carbon dioxide and hydrogen via aqueous reforming with co-existence of low level of carbon monoxide due to reverse water-gas-shift (R-WGS) reaction and subsequently, CO and/or CO2 and H-2 react to form CH4 via side reaction of methanation. Here Matlab language is employed to calculate the reaction heat, equilibrium constant and equilibrium molar fraction of each component through solving the non-linear equations. The calculation results suggest that the polylol reforming reaction is endothermic and but should be carried at low temperature to give very low level of CO content (dry basis) in the gas production. The results also demonstrate that low temperature favors the methanation, which should be limited kinetically during the operation. In addition, choosing system pressure slightly higher than the saturation water pressure is unfavorable to the R-WGS reaction but favorable to the low level of CO content, desirably. (c) 2006 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1727 / 1736
页数:10
相关论文
共 17 条
[1]  
CAR YL, 1999, CHEM PROPERTIES HDB, P4
[2]   Hydrogen from catalytic reforming of biomass-derived hydrocarbons in liquid water [J].
Cortright, RD ;
Davda, RR ;
Dumesic, JA .
NATURE, 2002, 418 (6901) :964-967
[3]   A review of catalytic issues and process conditions for renewable hydrogen and alkanes by aqueous-phase reforming of oxygenated hydrocarbons over supported metal catalysts [J].
Davda, RR ;
Shabaker, JW ;
Huber, GW ;
Cortright, RD ;
Dumesic, JA .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2005, 56 (1-2) :171-186
[4]   Catalytic reforming of oxygenated hydrocarbons for hydrogen with low levels of carbon monoxide [J].
Davda, RR ;
Dumesic, JA .
ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2003, 42 (34) :4068-4071
[5]   An overview of aqueous-phase catalytic processes for production of hydrogen and alkanes in a biorefinery [J].
Huber, GW ;
Dumesic, JA .
CATALYSIS TODAY, 2006, 111 (1-2) :119-132
[6]  
LIU G, 2002, HDB PROPERTIES ORGAN, P4
[7]  
MARGARDIA B, 1998, J CHEM THERMODYN, V20, P1353
[8]   A New Two-Constant Equation of State [J].
PENG, D ;
ROBINSON, DB .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1976, 15 (01) :59-64
[9]  
RICARDO RS, 2006, ANGEW CHEM INT EDIT, V45, P3982
[10]  
RUPALI RD, 2004, CHEM COMMUN, P36