Combined methanol reforming for hydrogen generation over monolithic catalysts

被引:76
作者
Lindström, B [1 ]
Agrell, J [1 ]
Pettersson, LJ [1 ]
机构
[1] Royal Inst Technol, KTH, Dept Chem Engn & Technol Chem Technol, SE-10044 Stockholm, Sweden
关键词
fuel cell vehicles; methanol reforming; hydrogen; monoliths; copper-based catalysts;
D O I
10.1016/S1385-8947(02)00112-2
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
An experimental investigation on hydrogen generation from methanol using monolithic catalysts is presented in this paper. The activity and carbon dioxide selectivity for the reforming of methanol over various binary copper-based materials, Cu/Cr, Cu/Zn and Cu/Zr, have been evaluated. The methanol reforming was performed using steam reforming and combined reforming (CMR, a combination of steam reforming and partial oxidation). The CMR process was carried out at two modes of operation: near auto-thermal and at slightly exothermal conditions. The catalysts have been characterized using BET surface area measurement, X-ray diffraction (XRD), temperature programmed reduction (TPR) and scanning electron microscopy (SEM-EDS). The results show that the choice of catalytic material has a great influence on the methanol conversion and carbon dioxide selectivity of the reforming reaction. The zinc-containing catalyst showed the highest activity for the steam reforming process, whereas the copper/chromium catalyst had the highest activity for the CMR process. The copper/zirconium catalyst had the highest CO2 selectivity for all the investigated process alternatives. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:91 / 101
页数:11
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