Autothermal methanol reforming for hydrogen production in fuel cell applications

被引:135
作者
Geissler, K [1 ]
Newson, E [1 ]
Vogel, F [1 ]
Truong, TB [1 ]
Hottinger, P [1 ]
Wokaun, A [1 ]
机构
[1] Paul Scherrer Inst, Lab Energy & Mat Cycles, CH-5232 Villigen, Switzerland
关键词
D O I
10.1039/b004881j
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
Fuel cell powered electric cars using on-board methanol reforming to produce a hydrogen-rich gas represent a low-emissions alternative to gasoline internal combustion engines (ICE). In order to exceed the well-to-wheel efficiencies of 17% for the gasoline ICE, high-efficiency fuel cells and methanol reformers must be developed. Catalytic autothermal reforming of methanol offers advantages over endothermic steam-reforming and exothermic partial oxidation. Microreactor testing of copper-containing catalysts was carried out in the temperature range between 250 and 330 degreesC showing nearly complete methanol conversion at 85% hydrogen yield. For the overall process a simplified model of the reaction network, consisting of the total oxidation of methanol, the reverse water-gas shift reaction, and the steam-reforming of methanol, is proposed. Individual kinetic measurements for the latter two reactions on a commercial Cu/ZnO/Al2O3 catalyst are presented.
引用
收藏
页码:289 / 293
页数:5
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