Stacked etched aluminum flow-through membranes for methanol steam reforming

被引:13
作者
Hiramatsu, Hiromi [1 ,3 ]
Sakurai, Makoto [1 ]
Maki, Tei [2 ,4 ]
Kameyama, Hideo [1 ]
机构
[1] Tokyo Univ Agr & Technol, Dept Chem Engn, 24-16 Naka Cho 2, Koganei, Tokyo 1848588, Japan
[2] Tokyo Univ Agr & Technol, Res Ctr Sci & Technol, Fuchu, Tokyo, Japan
[3] Japan Capacitor Ind Co Ltd, Dept Dev, 23-1 Musashinodai 1, Fussa, Tokyo 1970013, Japan
[4] JEOL Ltd, EM Applicat Dept, EM Business Unit, 1-2 Musashino 3, Akishima, Tokyo 1968558, Japan
关键词
Microreactor; Flow-through catalyst membrane reactor; Microchannel; Methanol steam reforming; Anodized alumina; SELECTIVE CATALYTIC-REDUCTION; HYDROGEN-PRODUCTION; NITRIC-OXIDE; MICROREACTOR; PROPENE; FOIL;
D O I
10.1016/j.ijhydene.2017.01.106
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
Electrochemical etching has been used to obtain aluminum foil with high surface area for use as electrodes in electrolytic capacitors. In this approach, direct current etching first generates straight penetrating microchannels, and then a second etching step enlarges the microchannel diameter. In the present work, we developed catalyst supports using aluminum etched with microchannels as a microreactor. The metal aluminum foil catalyst support obtained by etching contained microchannels with a diameter of 1.0-3.0 mu m (10,000-15,000 microchannels/mm(2)). We stacked membrane layers and evaluated their performance in methanol steam reforming. The performance of the reactors containing stacked membranes improved as the layer number increased. The microchannels in this catalytic membrane could be used as reaction channels, were easy to fabricate at low cost, and could be mass-produced continuously. This novel catalytic membrane support opens up new possibilities for practical fabrication of industrial materials. (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:9922 / 9929
页数:8
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