Thermodynamic study on hydrogen generation from different glycerol reforming processes

被引:62
作者
Luo, Nianjun
Zhao, Xun
Cao, Fahai
Xiao, Tiancun [1 ]
Fang, Dingye
机构
[1] E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
[2] E China Univ Sci & Technol, Inst Chem Technol, Shanghai 200237, Peoples R China
[3] Univ Oxford, Wolfson Catalysis Ctr, Inorgan Chem Lab, Oxford OX1 2JD, England
关键词
D O I
10.1021/ef070066g
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 work is to study the thermodynamic property of a glycerol aqueous reforming process to generate hydrogen for fuel cells. Three ways of processing glycerol have been considered: autothermal reforming, a combination of water aqueous reforming and oxidation; aqueous hydrogen peroxide reforming; and the water aqueous reforming process. Thermodynamic analysis on three of them has been carried out, and the results show that the side reaction of methanation in each process route leads to a dramatic decrease of hydrogen content in the gas product, which consequently should be limited kinetically. Comparison among them indicates that, in the absence of methanation, the hydrogen content produced from water aqueous reforming of glycerol is the highest, followed by that from autothermal reforming and that from aqueous hydrogen peroxide reforming. It has also been shown that the requirements of external energy input to sustain these reforming reactions appear inversely among them. Therefore, it can be concluded thermodynamically that the external energy can be reduced at the price of losing hydrogen yield due to the exothermic oxidation, which consumes hydrogen to release energy.
引用
收藏
页码:3505 / 3512
页数:8
相关论文
共 14 条
[1]   Energy efficient production of hydrogen and syngas from biomass: Development of low-temperature catalytic process for cellulose gasification [J].
Asadullah, M ;
Ito, SI ;
Kunimori, K ;
Yamada, M ;
Tomishige, K .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2002, 36 (20) :4476-4481
[2]   Economics of the clean fuel hydrogen in a novel autothermal reforming process [J].
Chen, ZX ;
Elnashaie, SSEH .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (13) :4834-4840
[3]   An integrated decision support framework for the assessment and analysis of hydrogen production pathways [J].
Chui, F ;
Elkamel, A ;
Fowler, M .
ENERGY & FUELS, 2006, 20 (01) :346-352
[4]   Hydrogen from catalytic reforming of biomass-derived hydrocarbons in liquid water [J].
Cortright, RD ;
Davda, RR ;
Dumesic, JA .
NATURE, 2002, 418 (6901) :964-967
[5]   Hydrogen by catalytic steam reforming of liquid byproducts from biomass thermoconversion processes [J].
Czernik, S ;
French, R ;
Feik, C ;
Chornet, E .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (17) :4209-4215
[6]   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
[7]   Renewable hydrogen from ethanol by autothermal reforming [J].
Deluga, GA ;
Salge, JR ;
Schmidt, LD ;
Verykios, XE .
SCIENCE, 2004, 303 (5660) :993-997
[8]   Raney Ni-Sn catalyst for H2 production from biomass-derived hydrocarbons [J].
Huber, GW ;
Shabaker, JW ;
Dumesic, JA .
SCIENCE, 2003, 300 (5628) :2075-2077
[9]   Thermodynamic analysis of aqueous-reforming of polylols for hydrogen generation [J].
Luo, Nianjun ;
Cao, Fahai ;
Zhao, Xun ;
Xiao, Tiancun ;
Fang, Dingye .
FUEL, 2007, 86 (12-13) :1727-1736
[10]   Biomass mixing in a fluidized bed biomass gasifier for hydrogen production [J].
Shen, Laihong ;
Xiao, Jun ;
Niklasson, Fredrik ;
Johnsson, Filip .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (1-2) :636-643