Effect of structural and acidity/basicity changes of CuO-CeO2 Catalysts on their activity for water-gas shift reaction

被引:70
作者
Djinovic, Petar [1 ]
Levec, Janez [1 ]
Pintar, Albin [1 ]
机构
[1] Natl Inst Chem, Lab Catalysis & Chem React Engn, SI-1001 Ljubljana, Slovenia
关键词
Cu-Ce mixed oxide catalysts; CuO loading; Calcination temperature; Water-gas shift reaction; Surface acidity/basicity;
D O I
10.1016/j.cattod.2008.05.032
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The objective of this work was to investigate the influence of CuO loading and catalyst pretreatment procedure to derive an optimal CuO-CeO2 Catalyst for the water-gas shift reaction (WGS), and to study in detail structure- and surface acidity-activity relationships. Catalyst samples prepared by coprecipitation and a 10, 15 and 20 mol% CuO content were examined by XRD, BET and TPR/TPD analyses and subjected to pulse WGS activity tests in the temperature range of 180-400 degrees C. Strong structure-activity dependence in the WGS reaction was observed for all catalyst samples. It was established that increasing CuO content has a positive effect on H-2 production during the WGS reaction, due to favored CeO2 reduction. Increasing Calcination temperature on the other hand reduces the BET surface area, induced by CuO sintering and agglomeration of CeO2 particles, resulting in a negative effect on H-2 production. Distinctive WGS activity dependence on surface acidity was observed and investigated. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:222 / 227
页数:6
相关论文
共 19 条
[1]   Dispersion, reduction and catalytic properties of copper oxide supported on Ce0.5Zr0.5O2 solid solution [J].
Chen, Hongliang ;
Zhu, Haiyang ;
Wu, Yong ;
Gao, Fei ;
Dong, Lin ;
Zhu, Junjie .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2006, 255 (1-2) :254-259
[2]   TPR and XRD studies of yttria-doped ceria/γ-alumina-supported copper oxide catalyst [J].
Dow, WP ;
Wang, YP ;
Huang, TJ .
APPLIED CATALYSIS A-GENERAL, 2000, 190 (1-2) :25-34
[3]   Structure-activity relationship in nanostructured copper-ceria-based preferential CO oxidation catalysts [J].
Gamarra, D. ;
Munuera, G. ;
Hungria, A. B. ;
Fernandez-Garcia, M. ;
Conesa, J. C. ;
Midgley, P. A. ;
Wang, X. Q. ;
Hanson, J. C. ;
Rodriguez, J. A. ;
Martinez-Arias, A. .
JOURNAL OF PHYSICAL CHEMISTRY C, 2007, 111 (29) :11026-11038
[4]   A comparative study of water-gas-shift reaction over ceria supported metallic catalysts [J].
Hilaire, S ;
Wang, X ;
Luo, T ;
Gorte, RJ ;
Wagner, J .
APPLIED CATALYSIS A-GENERAL, 2001, 215 (1-2) :271-278
[5]   Wet oxidation of phenol on Ce1-xCuxO2-δ catalyst [J].
Hocevar, S ;
Batista, J ;
Levec, J .
JOURNAL OF CATALYSIS, 1999, 184 (01) :39-48
[6]   Water-gas shift catalysis: kinetic isotope effect identifies surface formates in rate limiting step for Pt/ceria catalysts [J].
Jacobs, G ;
Khalid, S ;
Patterson, PM ;
Sparks, DE ;
Davis, BH .
APPLIED CATALYSIS A-GENERAL, 2004, 268 (1-2) :255-266
[7]   Determination of kinetic parameters for the water-gas shift reaction on copper catalysts under realistic conditions for fuel cell applications [J].
Koryabkina, NA ;
Phatak, AA ;
Ruettinger, WF ;
Farrauto, RJ ;
Ribeiro, FH .
JOURNAL OF CATALYSIS, 2003, 217 (01) :233-239
[8]   Reduction characteristics of copper oxide in cerium and zirconium oxide systems [J].
Kundakovic, L ;
Flytzani-Stephanopoulos, M .
APPLIED CATALYSIS A-GENERAL, 1998, 171 (01) :13-29
[9]   Supported base metal catalysts for the preferential oxidation of carbon monoxide in the presence of excess hydrogen (PROX) [J].
Mariño, F ;
Descorme, C ;
Duprez, D .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2005, 58 (3-4) :175-183
[10]   Preferential oxidation of CO in rich H2 over CuO/CeO2:: Details of selectivity and deactivation under the reactant stream [J].
Martinez-Arias, A. ;
Hungria, A. B. ;
Munuera, G. ;
Gamarra, D. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2006, 65 (3-4) :207-216