Ni-Cu catalysts supported on different materials were tested in ethanol steam reforming reaction for hydrogen production. These catalysts were evaluated at reaction temperature of 400 degrees C under atmospheric pressure. The reagents, with a water/ethanol molar ratio equal to 10, were fed at 70 dm(3)/(h g(cat)) (after vaporization). Analysis of the ethanol conversion, as well as evaluation and quantification of the reaction products, indicated the catalyst 10% Ni-1% Cu/Ce0.6Zr0.4O2 as the most appropriate for the ethanol steam reforming under investigated reaction conditions, among the studied catalysts. During 8 h of reaction this catalyst presented an average ethanol conversion of 43%, producing a high amount of H-2 by steam reforming and by ethanol decomposition and dehydrogenation parallel reactions. Steam reforming, among the observed reactions, was quantified by the presence of carbon dioxide. About 60% of the hydrogen was produced from ethanol steam reforming and 40% from parallel reactions. (C) 2009 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
机构:Univ Fed Rio de Janeiro, COPPE, Peq, Nucat, BR-21941 Rio De Janeiro, Brazil
Alberton, Andre L.
;
Souza, Mariana M. V. M.
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机构:Univ Fed Rio de Janeiro, COPPE, Peq, Nucat, BR-21941 Rio De Janeiro, Brazil
Souza, Mariana M. V. M.
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Schmal, Martin
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Univ Fed Rio de Janeiro, COPPE, Peq, Nucat, BR-21941 Rio De Janeiro, BrazilUniv Fed Rio de Janeiro, COPPE, Peq, Nucat, BR-21941 Rio De Janeiro, Brazil
机构:Univ Fed Rio de Janeiro, COPPE, Peq, Nucat, BR-21941 Rio De Janeiro, Brazil
Alberton, Andre L.
;
Souza, Mariana M. V. M.
论文数: 0引用数: 0
h-index: 0
机构:Univ Fed Rio de Janeiro, COPPE, Peq, Nucat, BR-21941 Rio De Janeiro, Brazil
Souza, Mariana M. V. M.
;
Schmal, Martin
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h-index: 0
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Univ Fed Rio de Janeiro, COPPE, Peq, Nucat, BR-21941 Rio De Janeiro, BrazilUniv Fed Rio de Janeiro, COPPE, Peq, Nucat, BR-21941 Rio De Janeiro, Brazil