Ethanol steam reforming over rhodium and cobalt-based catalysts: Effect of the support

被引:50
|
作者
Moura, Jadson S. [1 ]
Souza, Marluce O. G. [2 ]
Bellido, Jorge David A. [3 ]
Assaf, Elisabete M. [3 ]
Opportus, Marcelo [4 ]
Reyes, Patricio [4 ]
Rangel, Maria do Carmo [1 ]
机构
[1] Univ Fed Bahia, GECCAT Gp Estudos Cinet & Catalise, Inst Quim, BR-40170280 Salvador, BA, Brazil
[2] Univ Estado Bahia, Dept Ciencias Exatas & Terra, BR-41195001 Salvador, BA, Brazil
[3] Univ Sao Paulo, Inst Quim Sao Carlos, BR-13560970 Sao Carlos, SP, Brazil
[4] Univ Concepcion, Fac Ciencias Quim, Concepcion, Chile
关键词
Hydrogen; Ethanol; Rhodium; Cobalt; Hydrotalcite; Steam reforming; WATER-GAS SHIFT; HYDROGEN-PRODUCTION; NI; NICKEL; RH; STABILITY; MAGNESIUM; PRECURSOR; OXIDES; FE;
D O I
10.1016/j.ijhydene.2011.10.112
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
The effect of support on the properties of rhodium and cobalt-based catalysts for ethanol steam reforming was studied in this work, by comparing the use of magnesia, alumina and Mg-Al oxide (obtained from hydrotalcite) as supports. It was found that metallic rhodium particles with around 2.4-2.6 nm were formed on all supports, but Mg-Al oxide led to the narrowest particles size distribution; cobalt was supposed to be located on the support, affecting its acidity. Rhodium interacts strongly with the support in the order: alumina> Mg-Al oxide > magnesia. The magnesium-containing catalysts showed low ethene selectivity and high hydrogen selectivity while the alumina-based ones showed high ethene selectivity, assigned to the Lewis sites of alumina. The Mg-Al oxide-supported rhodium and cobalt catalyst was the most promising sample to produce hydrogen by ethanol reforming, showing the highest hydrogen yield, low ethene selectivity and high specific surface area during reaction. Copyright (C) 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:3213 / 3224
页数:12
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