High temperature water-gas shift Cu catalysts supported on Ce-Al containing materials for the production of hydrogen using simulated coal-derived syngas

被引:14
作者
Sun, Y. [1 ]
Hla, S. S. [2 ]
Duffy, G. J. [1 ]
Cousins, A. J. [2 ]
French, D. [3 ]
Morpeth, L. D. [2 ]
Edwards, J. H. [1 ]
Roberts, D. G. [2 ]
机构
[1] CSIRO Energy Technol, Newcastle, NSW 2300, Australia
[2] CSIRO Energy Technol, Pullenvale, Qld 4069, Australia
[3] CSIRO Energy Technol, Bangor, NSW 2234, Australia
关键词
High temperature water-gas shift (HT WGS) catalyst; Ce-La-Al containing Cu catalysts; Hydrogen; Coal gasification; MIXED-OXIDE; CUO-CEO2; CATALYSTS; CU-CEO2; CERIA-ALUMINA; PERFORMANCE; OXIDATION; COPPER; STABILITY;
D O I
10.1016/j.catcom.2010.09.025
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
Novel Cu-based catalysts supported on both Ce-La-Al and Ce-Zr-Al supports were investigated for the water-gas shift reaction in the temperature range 450 to 600 C Ce-La-Al containing Cu catalysts exhibited high activity and stability for the high temperature water-gas shift reaction with catalyst 10%Cu/(36 8% CeO2 + 30 2%LaOx + 33 0%AlOx) (CE18) achieving the highest activity with 15 5% CO conversion at 600 C and atmospheric pressure higher than its counterpart Ce-Zr-Al containing Cu catalyst This high activity and stability may originate from the synergistic effect of the interaction between Cu and catalyst support the redox behaviour of catalyst support as well as the stabilizing effect of Al2O3 Crown Copyright (C) 2010 Published by Elsevier B V All rights reserved
引用
收藏
页码:304 / 309
页数:6
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