Compact string reactor for autothermal hydrogen production

被引:46
作者
Horny, C. [1 ]
Renken, A. [1 ]
Kiwi-Minsker, L. [1 ]
机构
[1] Ecole Polytech Fed Lausanne, LGRC, Ecole Polytech Fed Lausanne, CH-1015 Lausanne, Switzerland
关键词
autothermal hydrogen production; methanol; oxidative steam-reforming; brass-wire catalysts; micro-structured reactor; hot-spot; Raney metal;
D O I
10.1016/j.cattod.2006.07.003
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
This study addresses the development of a compact reactor for oxidative steam-reforming of methanol (OSRM) to produce hydrogen in autothermal mode for fuel cells. The string reactor uses catalytically active brass wires with a diameter of 500 mu m placed in parallel into a tube. The micro-channels in the reactor for gases are formed between the wires presenting hydrodynamics similar to the one in multi-channel micro-reactors. Due to the high thermal conductivity of brass, the heat generated during methanol oxidation at the reactor entrance is transferred to the zone of the endothermic steam-reforming. The catalysts are prepared by Al-alloy formation on the surface of the brass wires followed by the partial leaching of Al. The catalyst presents a porous layer with the morphology of Raney metals and the chemical composition consistent with the Cu/Zn/Al-mixed oxide. The catalyst surface was additionally modified by incorporating chromium leading to Cr/Cu-spinel. This decreases the degree of the reduction of copper oxide and sintering leading to a stable catalyst. The catalyst was tested in OSRM showing high activity and selectivity to carbon dioxide and hydrogen. The string reactor presents nearly isothermal profile since the temperatures gradient within the reactor length is about 3 K. Micro-structured string reactor presents a short start-up and a fast transient behavior showing a rapid temperature change when adjusting the oxygen amount introduced into the reactor. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:45 / 53
页数:9
相关论文
共 49 条
  • [1] 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
  • [2] Production of hydrogen from methanol over binary Cu/ZnO catalysts - Part II. Catalytic activity and reaction pathways
    Agrell, J
    Boutonnet, M
    Fierro, JLG
    [J]. APPLIED CATALYSIS A-GENERAL, 2003, 253 (01) : 213 - 223
  • [3] Production of hydrogen from methanol over binary Cu/ZnO catalysts -: Part I.: Catalyst preparation and characterisation
    Agrell, J
    Boutonnet, M
    Melián-Cabrera, I
    Fierro, JLG
    [J]. APPLIED CATALYSIS A-GENERAL, 2003, 253 (01) : 201 - 211
  • [4] Steam reforming of methanol over a Cu/ZnO/Al2O3 catalyst:: a kinetic analysis and strategies for suppression of CO formation
    Agrell, J
    Birgersson, H
    Boutonnet, M
    [J]. JOURNAL OF POWER SOURCES, 2002, 106 (1-2) : 249 - 257
  • [5] Partial oxidation of methanol to produce hydrogen over Cu-Zn-based catalysts
    Alejo, L
    Lago, R
    Pena, MA
    Fierro, JLG
    [J]. APPLIED CATALYSIS A-GENERAL, 1997, 162 (1-2) : 281 - 297
  • [6] AMPHLETT JC, 1994, STUD SURF SCI CATAL, V81, P409
  • [7] 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
  • [8] XPS and TPR examinations of γ-alumina-supported Pd-Cu catalysts
    Batista, J
    Pintar, A
    Mandrino, D
    Jenko, M
    Martin, V
    [J]. APPLIED CATALYSIS A-GENERAL, 2001, 206 (01) : 113 - 124
  • [9] Methanol reforming for fuel-cell applications: development of zirconia-containing Cu-Zn-Al catalysts
    Breen, JP
    Ross, JRH
    [J]. CATALYSIS TODAY, 1999, 51 (3-4) : 521 - 533
  • [10] Mechanistic aspects of the steam reforming of methanol over a CuO/ZnO/ZrO2/Al2O3 catalyst
    Breen, JP
    Meunier, FC
    Ross, JRH
    [J]. CHEMICAL COMMUNICATIONS, 1999, (22) : 2247 - 2248