Hydrogen production by oxidative methanol reforming on Pd/ZnO: Catalyst deactivation

被引:64
作者
Liu, ST [1 ]
Takahashi, K [1 ]
Fuchigami, K [1 ]
Uematsu, K [1 ]
机构
[1] Ishikawajima Harima Heavy Ind Co Ltd, Tech Res Lab, Yokohama, Kanagawa 2358501, Japan
关键词
catalyst deactivation; hydrogen production; oxidative steam reforming; methanol; palladium; zinc oxide;
D O I
10.1016/j.apcata.2005.10.012
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 durability performance of Pd/ZnO for oxidative methanol reforming has been investigated. While Cu/ZnO lost its activity with a constant selectivity of CO formation, Pd/ZnO exhibited a more stable activity, but with increasing CO production throughout the reaction time on stream. Characterization of the catalyst using XRD and XPS revealed the formation of a Pd-Zn alloy, which was thought to be essential for the selective production of hydrogen. Based on the reaction and the catalyst characterization results, two routes were supposed for the deactivation of Pd/ZnO catalyst: surface fouling by deposited carbon and surface oxidation of the Pd-Zn alloy, breaking down the Pd-Zn alloy to produce more elemental Pd on a ZnO support. The catalyst can be regenerated in a H-2 reducing atmosphere at higher temperatures and in a diluted 02 atmosphere at lower temperatures. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:58 / 65
页数:8
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