A low-temperature co-fired ceramic micro-reactor system for high-efficiency on-site hydrogen production

被引:16
|
作者
Jiang, Bo [1 ,2 ]
Maeder, Thomas [2 ]
Santis-Alvarez, Alejandro J. [3 ]
Poulikakos, Dimos [3 ]
Muralt, Paul [1 ]
机构
[1] Ecole Polytech Fed Lausanne, Ceram Lab, CH-1015 Lausanne, Switzerland
[2] Ecole Polytech Fed Lausanne, Lab Microengn Mfg, CH-1015 Lausanne, Switzerland
[3] ETH, Lab Thermodynam Emerging Technol, Zurich, Switzerland
基金
瑞士国家科学基金会;
关键词
LTCC; Micro-reactor; Hydrogen production; Solid oxide fuel cells; OXIDE FUEL-CELL; CATALYTIC PARTIAL OXIDATION; PORTABLE POWER PRODUCTION; N-BUTANE; MICROSTRUCTURED REACTORS; MICROCHANNEL REACTORS; PACKED-BED; MICROREACTOR; PROPANE; PERFORMANCE;
D O I
10.1016/j.jpowsour.2014.09.084
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
A ceramic-based, meso-scale fuel processor for on-board production of syngas fuel was demonstrated for applications in micro-scale solid-oxide fuel cells (mu-SOFCs). The processor had a total dimension of 12 mm x 40 mm x 2 mm, the gas reforming micro reactor occupying the hot end of a cantilever had outer dimensions of 12 x 18 mm. The device was fabricated through a novel progressive lamination process in low-temperature co-fired ceramic (LTCC) technology. Both, heating function and desired fluidic structures were integrated monolithically into the processor. Using catalytic partial oxidation of a hydrocarbon fuel (propane) as a reaction model, a thermally self-sustaining hydrogen production was achieved. The output flow is sufficiently high to drive an optimized single membrane mu SOFC cell of about the same footprint as the micro reactor. Microsystem design, fabrication, catalyst integration as well as the chemical characterization are discussed in detail. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:1202 / 1217
页数:16
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