Zirconia supported catalysts for bioethanol steam reforming:: Effect of active phase and zirconia structure

被引:67
作者
Benito, M. [1 ]
Padilla, R. [1 ]
Rodriguez, L. [1 ]
Sanz, J. L. [1 ]
Daza, L. [1 ]
机构
[1] CSIC, Inst Catalisis & Petroleoquim, E-28049 Madrid, Spain
关键词
bioethanol; reforming; bio-energy; hydrogen; fuel processor; fuel cell;
D O I
10.1016/j.jpowsour.2007.01.047
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
Three new catalysts have been prepared in order to study the active phase influence in ethanol steam reforming reaction. Nickel, cobalt and copper were the active phases selected and were supported on zirconia with monoclinic and tetragonal structure, respectively. To characterize the behaviour of the catalysts in reaction conditions a study of catalytic activity with temperature was performed. The highest activity values were obtained at 973 K where nickel and cobalt based catalysts achieved an ethanol conversion of 100% and a selectivity to hydrogen close to 70%. Nickel supported on tetragonal zirconia exhibited the highest hydrogen production efficiency, higher than 4.5 mol H-2/mol EtOH fed. The influence of stearn/carbon (S/C) ratio on product distribution was another parameter studied between the range 3.2-6.5. Nickel supported on tetragonal zirconia at S/C = 3.2 operated at 973 K without by-product production such as ethylene or acetaldehyde. In order to consider a further application in an ethanol processor, a long-term reaction experiment was performed at 973 K, S/C = 3.2 and atmospheric pressure. After 60 h, nickel supported on tetragonal zirconia exhibited high stability and selectivity to hydrogen production. (c) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:167 / 176
页数:10
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