Effect of process variables on Pt/CeO2 catalyst behaviour for the PROX reaction

被引:89
|
作者
Ayastuy, J. L. [1 ]
Gil-Rodriguez, A. [1 ]
Gonzalez-Marcos, M. P. [1 ]
Gutierrez-Ortiz, M. A. [1 ]
机构
[1] Univ Basque Country, Euskal Herriko Herriko, Grp Chem Technol Environm Sustainabil, Dept Chem Engn,Fac Sci & Technol, E-48080 Bilbao, Spain
关键词
cerium oxide; Pt; CO oxidation; selective CO oxidation; catalyst yield;
D O I
10.1016/j.ijhydene.2006.04.008
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
A Pt/CeO2 catalyst has been evaluated for CO oxidation, both in the absence of H-2 and in H-2-rich feedstreams. The catalyst shows high activity and selectivity at temperatures as low as 80 degrees C, what makes it a viable catalyst for the selective depletion of CO in the temperature range at which PEMFC operate. The effect of: oxygen excess during operation (lambda), the presence of either CO2 (5%), H2O (5%) or both in the feedstream, and the spatial time, on catalyst activity and selectivity has been evaluated. A lambda value of at least 2.25 was required for achieving total CO conversion, which occurs in the temperature range of 80-100 degrees C, being the selectivity practically stable at 44%. The presence of CO2 slight activates the catalyst, while steam inhibits catalyst activity. Water gas shift reaction contribution to CO oxidation was checked to be negligible in the 25-200 degrees C range. (c) 2006 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:2231 / 2242
页数:12
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