Hydrogen production from ethanol steam reforming in a micro-channel reactor

Ethanol steam reforming was studied over a supported Ir/CeO 2 catalyst in a micro-channel structured reactor. The catalyst coating was deposited on the channel walls and showed a remarkably high homogeneity and an excellent adherence to the stainless steel substrate, leading to stable performance du...

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Veröffentlicht in:International journal of hydrogen energy 2010-02, Vol.35 (3), p.1152-1159
Hauptverfasser: Cai, Weijie, Wang, Fagen, van Veen, Andre, Descorme, Claude, Schuurman, Yves, Shen, Wenjie, Mirodatos, Claude
Format: Artikel
Sprache:eng
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Zusammenfassung:Ethanol steam reforming was studied over a supported Ir/CeO 2 catalyst in a micro-channel structured reactor. The catalyst coating was deposited on the channel walls and showed a remarkably high homogeneity and an excellent adherence to the stainless steel substrate, leading to stable performance during long-term runs. Hydrogen yields exceeding 40 L H2 g cat −1 h −1 were achieved during testing with partial ethanol conversion of 65% and a residence time in the order of a few milliseconds. This hydrogen productivity was found significantly higher than in a comparable conventional fixed-bed reactor hence being extremely promising for hydrogen production in micro fuel cell applications.
ISSN:0360-3199
1879-3487
DOI:10.1016/j.ijhydene.2009.11.104