4.7 Article Proceedings Paper

Selective production of hydrogen by steam reforming of bio-ethanol

Journal

CATALYSIS TODAY
Volume 176, Issue 1, Pages 28-35

Publisher

ELSEVIER SCIENCE BV
DOI: 10.1016/j.cattod.2011.06.006

Keywords

Hydrogen; Bio-ethanol; Steam reforming; Cobalt catalyst; Renewable fuel

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Experimental results of catalytic activity, selectivity and coking phenomenon on co-precipitated cobalt catalysts with the ZnO-Al(2)O(3) support in the steam reforming of ethanol (SRE) are reported. The influence of the cobalt active phase content (9-41 wt.%) and the reaction temperature (350-600 degrees C) was the point at issue. From the point of view of activity and selectivity, temperatures 420. C and higher favoured steam reforming of ethanol on supported cobalt catalysts. At these temperatures the conversion of ethanol reached 100%, simultaneously the hydrogen yield achieved the level of above 5 mol of H(2) formed from 1 mol of EtOH introduced to the reaction, as well as the selectivity of carbon monoxide formation was depressed to 2-3%. However, taking into account possibility of coking of catalysts, the optimum temperature of the SRE is 420 degrees C. The catalyst containing 24 wt.% of cobalt was the most effective one. The obtained results are very important in the aspect of electricity generation in fuel cells feed with a reformate gas. (C) 2011 Elsevier B.V. All rights reserved.

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