Onboard fuel conversion for hydrogen-fuel-cell-driven vehicles

被引:549
作者
Trimm, DL [1 ]
Önsan, ZI
机构
[1] Univ New S Wales, Sch Chem Engn & Ind Chem, Sydney, NSW 2052, Australia
[2] Bogazici Univ, Dept Chem Engn, TR-80815 Bebek, Istanbul, Turkey
来源
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING | 2001年 / 43卷 / 1-2期
关键词
hydrogen; fuel cell; onboard hydrogen generation; hydrocarbon partial oxidation;
D O I
10.1081/CR-100104386
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Increasingly stringent legislation controls emissions from internal combustion engines to the point where alternative power sources for vehicles are necessary. The hydrogen fuel cell is one promising option, but the nature of the gas is such that the conversion of other fuels to hydrogen on board the vehicle is necessary. The conversion of methanol, methane, propane, and octane to hydrogen is reviewed. A combination of oxidation and steam reforming (indirect partial oxidation) or direct partial oxidation are the most promising processes. Indirect partial oxidation involves combustion of part of the fuel to produce sufficient heat to drive the endothermic steam reforming reaction. Direct partial oxidation is favored only at high temperatures and short residence times but is highly selective. However, indirect partial oxidation is shown to be the preferred process for all, fuels. The product gases can be taken through a water-gas shift reactor, but still retain similar to2% carbon monoxide, which poisons fuel-cell catalysts. Selective oxidation is the preferred route to removal of residual carbon monoxide. Low-temperature oxidation in the absence and presence of an excess of hydrogen is reviewed. An-based catalysts show much promise, but precious metal catalysts such as Pt/zeolite have some advantages.
引用
收藏
页码:31 / 84
页数:54
相关论文
共 217 条
  • [1] Acres G., 1966, PLATINUM MET REV, V10, P60
  • [2] COPPER-CATALYSTS FOR THE STEAM REFORMING OF METHANOL - ANALYSIS OF THE PREPARATION VARIABLES
    AGARAS, H
    CERRELLA, G
    LABORDE, MA
    [J]. APPLIED CATALYSIS, 1988, 45 (01): : 53 - 60
  • [3] HYDROGEN-PRODUCTION BY THE CATALYTIC STEAM REFORMING OF METHANOL .2. KINETICS OF METHANOL DECOMPOSITION USING GIRDLER G66B CATALYST
    AMPHLETT, JC
    EVANS, MJ
    MANN, RF
    WEIR, RD
    [J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1985, 63 (04) : 605 - 611
  • [4] [Anonymous], 1989, CATALYST HDB
  • [5] ENVIRONMENTAL CATALYSIS
    ARMOR, JN
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 1992, 1 (04) : 221 - 256
  • [6] PARTIAL OXIDATION OF METHANE TO SYNTHESIS GAS-USING CARBON-DIOXIDE
    ASHCROFT, AT
    CHEETHAM, AK
    GREEN, MLH
    VERNON, PDF
    [J]. NATURE, 1991, 352 (6332) : 225 - 226
  • [7] AVCI AK, 2000, P 12 INT C CAT AMST, P2753
  • [8] AVCI AK, UNPUB
  • [9] *B JOHNS CO, 1972, GAS MAK NAT GAS
  • [10] CATALYTIC COMBUSTION OF METHANE OVER SUPPORTED PALLADIUM CATALYSTS .1. ALUMINA SUPPORTED CATALYSTS
    BALDWIN, TR
    BURCH, R
    [J]. APPLIED CATALYSIS, 1990, 66 (02): : 337 - 358