Reaction-relevant gold structures in the low temperature water-gas shift reaction on Au-CeO2

被引:134
作者
Deng, Weiling [1 ]
Frenkel, Anatoly I. [2 ]
Si, Rui [1 ]
Flytzani-Stephanopoulos, Maria [1 ]
机构
[1] Tufts Univ, Dept Chem & Biol Engn, Medford, MA 02155 USA
[2] Yeshiva Univ, Dept Phys, New York, NY 10016 USA
基金
美国国家科学基金会;
关键词
D O I
10.1021/jp800075y
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
Combined in situ X-ray absorption near-edge structure (XANES) and extended X-ray absorption fine structure (EXAFS) studies have been conducted to follow gold structural changes of low-content (< 1 % Au) gold-ceria catalysts in water-gas shift (WGS) reaction tests at 100 and 200 degrees C; and after heating the used catalysts in oxygen gas at 150 degrees C. Gold in the fresh (400 degrees C-calcined) material was atomically dispersed in cerium oxide. Under WGS reaction conditions, reduction of the oxidized gold species was observed, accompanied by gradual gold aggregation. The Au-Au coordination number is zero for the fresh material, but increases with the reaction temperature, to 6.5 +/- 2.4 (after use at 100 degrees C) and to 8.7 +/- 1.5 (after 200 degrees C) in a gas mixture containing 5% CO- 3% H2O in helium. The second important parameter is the reaction gas composition which determines the extent of Au-O reduction. The lower the reduction potential of the reaction gas mixture, the more oxidized the gold is in the used catalyst, and the higher its activity. The maximum activity of Au-CeO2 was that of the fully dispersed Au-O-Ce fresh material. Loss of surface oxygen took place during reaction, as measured by H-2-TPR of the used samples, and it was commensurate with the activity loss. Attempts to reoxidize and redisperse the gold by heating in oxygen gas at 150 degrees C were not effective. However, we report here that complete recovery of the surface oxygen amount and redispersion of gold in ceria was possible after a 400 degrees C- oxygen treatment of both the 100 degrees C- and 200 degrees C- used catalyst samples, with concomitant recovery of the initial catalyst activity. These tests were conducted by consecutive H-2-TPP/steady-state catalyst activity measurements in the same microreactor.
引用
收藏
页码:12834 / 12840
页数:7
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