Process development of hydrogenous gas production for PEFC from biogas

被引:43
作者
Zhang, ZG [1 ]
Xu, GW [1 ]
Chen, X [1 ]
Honda, K [1 ]
Yoshida, T [1 ]
机构
[1] Natl Inst Adv Ind Sci & Technol, Sapporo, Hokkaido 0628517, Japan
关键词
biogas; steam reforming; selective CO oxidation; hydrogen; polymer electrolyte fuel cell (PEFC);
D O I
10.1016/j.fuproc.2003.10.017
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A laboratory-scale gas processor that integrates four successive catalytic reactions: steam reforming of methane, high- and low-temperature water gas shifts and selective oxidation of carbon monoxide, was designed and tested in this study to produce hydrogen-rich gas with CO < 10 ppm from a clean model biogas having a constant molar ratio of CH4/CO2 = 1.5:1.0 for a 50-W class polymer electrolyte fuel cell (PEFC) stack. All tests to determine the optimum operating condition of each of the reactions were conducted over commercial catalysts in their manufactured shapes and sizes in order to obtain data practically valuable for scale-up of the processor. A 7-h continuous test was also finally conducted to confirm the stabilities of the catalysts and reliability of the processor. The resulting data has shown that the proposed processor is indeed functional to produce a hydrogen-rich gas with 60-70% H-2 of about 1.6 l/min at PEFC-fuel standard from the clean model biogas. © 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:1213 / 1229
页数:17
相关论文
共 15 条
[1]   THERMODYNAMIC ANALYSIS OF HYDROGEN-PRODUCTION FROM BIOGAS FOR PHOSPHORIC-ACID FUEL-CELL [J].
CHAWLA, SK ;
GHOSH, KK .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1992, 17 (06) :405-412
[2]   Evaluation and modelling of a CO selective oxidation reactor for solid polymer fuel cell automotive applications [J].
Dudfield, CD ;
Chen, R ;
Adcock, PL .
JOURNAL OF POWER SOURCES, 2000, 85 (02) :237-244
[3]   A compact CO selective oxidation reactor for solid polymer fuel cell powered vehicle application [J].
Dudfield, CD ;
Chen, R ;
Adcock, PL .
JOURNAL OF POWER SOURCES, 2000, 86 (1-2) :214-222
[4]   Steam reforming of a clean model biogas over Ni/Al2O3 in fluidized- and fixed-bed reactors [J].
Effendi, A ;
Zhang, ZG ;
Hellgardt, K ;
Honda, K ;
Yoshida, T .
CATALYSIS TODAY, 2002, 77 (03) :181-189
[5]   KINETICS OF THE WATER-GAS SHIFT REACTION OVER SEVERAL ALKANE ACTIVATION AND WATER-GAS SHIFT CATALYSTS [J].
KEISKI, RL ;
DESPONDS, O ;
CHANG, YF ;
SOMORJAI, GA .
APPLIED CATALYSIS A-GENERAL, 1993, 101 (02) :317-338
[6]   Selective catalytic oxidation of CO in H2:: Fuel cell applications [J].
Korotkikh, O ;
Farrauto, R .
CATALYSIS TODAY, 2000, 62 (2-3) :249-254
[7]   FUEL-CELLS FOR TRANSPORTATION [J].
LEMONS, RA .
JOURNAL OF POWER SOURCES, 1990, 29 (1-2) :251-264
[8]   Biogas plants in Denmark:: technological and economic developments [J].
Mæng, H ;
Lund, H ;
Hvelplund, F .
APPLIED ENERGY, 1999, 64 (1-4) :195-206
[9]   CARBON-MONOXIDE REMOVAL FROM HYDROGEN-RICH FUEL-CELL FEEDSTREAMS BY SELECTIVE CATALYTIC-OXIDATION [J].
OH, SH ;
SINKEVITCH, RM .
JOURNAL OF CATALYSIS, 1993, 142 (01) :254-262
[10]   CATALYTIC STEAM REFORMING. [J].
Rostrup-Nielsen, Jens R. .
Catalysis: Science and Technology, 1984, 5 :1-117