Ultrahigh temperature water gas shift catalysts to increase hydrogen yield from biomass gasification

被引:41
作者
Haryanto, Agus [1 ]
Fernando, Sandun [1 ]
Adhikari, Sushil [1 ]
机构
[1] Mississippi State Univ, Dept Agr & Biol Engn, Mississippi State, MS 39762 USA
关键词
hydrogen; biomass gasification; ultrahigh temperature; water gas shift (WGS);
D O I
10.1016/j.cattod.2006.09.039
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Noble metal (Rh, Pt, Pd, Ir, Ru, and Ag) and Ni catalysts supported on CeO2-Al2O3 were investigated for water gas shift reaction at ultrahigh temperatures. Pt/CeO2-Al2O3 and Ru/CeO2-Al2O3 demonstrated as the best catalysts in terms of activity, hydrogen yield and hydrogen selectivity. At 700 degrees C and steam to CO ratio of 5.2:1, Pt/CeO2-Al2O3 converted 76.3% of CO with 94.7% of hydrogen selectivity. At the same conditions, the activity and hydrogen selectivity for Ru/CeO2-Al2O3 were 63.9% and 85.6%, respectively. Both catalysts showed a good stability over 9 h of continuous operation. However, both catalysts showed slight deactivation during the test period. The study revealed that Pt/CeO2-Al2O3 and Ru/CeO2-Al2O3 were excellent ultrahigh temperature water gas shift catalysts, which can be coupled with biomass gasification in a downstream reactor. (c) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:269 / 274
页数:6
相关论文
共 27 条
[1]   Hydrogen from renewable resources - the hundred year commitment [J].
Adamson, KA .
ENERGY POLICY, 2004, 32 (10) :1231-1242
[2]  
BOWEN DA, 2003, FY 2003 ANN PROGR RE, P78
[3]   Production of hydrogen and/or syngas (H2+CO) via steam gasification of biomass-derived chars [J].
Chaudhari, ST ;
Dalai, AK ;
Bakhshi, NN .
ENERGY & FUELS, 2003, 17 (04) :1062-1067
[4]   Utilisation of biomass for the supply of energy carriers [J].
Claassen, PAM ;
van Lier, JB ;
Contreras, AML ;
van Niel, EWJ ;
Sijtsma, L ;
Stams, AJM ;
de Vries, SS ;
Weusthuis, RA .
APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 1999, 52 (06) :741-755
[5]   Active nonmetallic Au and Pt species on ceria-based water-gas shift catalysts [J].
Fu, Q ;
Saltsburg, H ;
Flytzani-Stephanopoulos, M .
SCIENCE, 2003, 301 (5635) :935-938
[6]   Water-gas shift reaction kinetics over μ-structured Pt/CeO2/Al2O3 catalysts [J].
Germani, G ;
Schuurman, Y .
AICHE JOURNAL, 2006, 52 (05) :1806-1813
[7]   Study of the origin of the deactivation of a Pt/CeO2 catalyst during reverse water gas shift (RWGS) reaction [J].
Goguet, A ;
Meunier, F ;
Breen, JP ;
Burch, R ;
Petch, MI ;
Ghenciu, AF .
JOURNAL OF CATALYSIS, 2004, 226 (02) :382-392
[8]  
HARYANTO A, 2006, ACAS NAT M ATL APR 2
[9]   A comparative study of water-gas-shift reaction over ceria-supported metallic catalysts (vol 215, pg 271, 2001) [J].
Hilaire, S ;
Wang, X ;
Luo, T ;
Gorte, RJ ;
Wagner, J .
APPLIED CATALYSIS A-GENERAL, 2004, 258 (02) :269-+
[10]   Low-temperature water-gas shift: impact of Pt promoter loading on the partial reduction of ceria and consequences for catalyst design [J].
Jacobs, G ;
Graham, UM ;
Chenu, E ;
Patterson, PM ;
Dozier, A ;
Davis, BH .
JOURNAL OF CATALYSIS, 2005, 229 (02) :499-512