Steam reforming and oxidative steam reforming of methanol over CuO-CeO2 catalysts

被引:103
作者
Udani, P. P. C. [1 ]
Gunawardana, P. V. D. S. [1 ]
Lee, Hyun Chan [1 ]
Kim, Dong Hyun [1 ]
机构
[1] Kyungpook Natl Univ, Dept Chem Engn, Taegu 702701, South Korea
关键词
Steam reforming; Oxidative steam reforming; Methanol; CuO-CeO2; catalyst; Coprecipitation method; Optimum composition; COPPER-BASED CATALYSTS; WATER-GAS SHIFT; HYDROGEN-PRODUCTION; PREFERENTIAL OXIDATION; SELECTIVE PRODUCTION; ALUMINA CATALYSTS; OXIDE CATALYSTS; CO OXIDATION; CEO2; COPRECIPITATION;
D O I
10.1016/j.ijhydene.2009.07.035
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
Steam reforming (SRM) and oxidative steam reforming of methanol (OSRM) were carried out over a series of coprecipitated CuO-CeO2 catalysts with varying copper content in the range of 30-80 at.% Cu (= 100 x Cu/(Cu + Ce)). The effects of copper content, reaction temperature and O-2 concentration on catalytic activity were investigated. The activity of CuO-CeO2 catalysts for SRM and OSRM increased with the copper content and 70 at.% Cuo-CeO2 catalyst showed the highest activity in the temperature range of 160-300 degrees C for both SRM and OSRM. After SRM or OSRM, the copper species in the catalysts observed by XRD were mainly metallic copper with small amount of CuO and Cu2O, an indication that metallic copper is an active species in the catalysis of both SRM and OSRM. It was observed that the methanol conversion increased considerably with the addition Of O-2 into the feed stream, indicating that the partial oxidation of methanol (POM) is much faster than SRM. The optimum 70 at% CuO-CeO2 catalyst showed stable activities for both SRM and OSRM reactions at 300 degrees C. (C) 2009 Professor T. Nejat Veziroglu. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:7648 / 7655
页数:8
相关论文
共 42 条
[1]   Selective CO oxidation over CuO-CeO2 catalysts prepared via the urea-nitrate combustion method [J].
Avgouropoulos, G ;
Ioannides, T .
APPLIED CATALYSIS A-GENERAL, 2003, 244 (01) :155-167
[2]   Hydrogen from methanol steam-reforming over Cu-based catalysts with and without Pd promotion [J].
Bichon, P. ;
Asheim, A. ;
Jordal, A. ;
Sperle, T. ;
Fathi, M. ;
Holmen, A. ;
Blekkan, E. A. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2007, 32 (12) :1799-1805
[3]   Steam reforming of methanol over highly active Pd/ZnO catalyst [J].
Chin, YH ;
Dagle, R ;
Hu, JL ;
Dohnalkova, AC ;
Wang, Y .
CATALYSIS TODAY, 2002, 77 (1-2) :79-88
[4]   Synthesis of highly active CuO-CeO2 nanocomposites for preferential oxidation of carbon monoxide at low temperatures [J].
Chung, Liang-Chor ;
Yeh, Chuln-Tih .
CATALYSIS COMMUNICATIONS, 2008, 9 (05) :670-674
[5]   Calcination temperature and CuO loading dependence on CuO-CeO2 catalyst activity for water-gas shift reaction [J].
Djinovic, Petar ;
Batista, Jurka ;
Pintar, Albin .
APPLIED CATALYSIS A-GENERAL, 2008, 347 (01) :23-33
[6]   A comparative study on the performance of mesoporous SBA-15 supported Pd-Zn catalysts in partial oxidation and steam reforming of methanol for hydrogen production [J].
Eswaramoorthi, I. ;
Dalai, A. K. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2009, 34 (06) :2580-2590
[7]   Kinetic study of the reverse water-gas shift reaction over CuO/ZnO/Al2O3 catalysts [J].
Gines, MJL ;
Marchi, AJ ;
Apesteguia, CR .
APPLIED CATALYSIS A-GENERAL, 1997, 154 (1-2) :155-171
[8]   Performance of copper-ceria catalysts for water gas shift reaction in medium temperature range [J].
Gunawardana, P. V. D. S. ;
Lee, Hyun Chan ;
Kim, Dong Hyun .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2009, 34 (03) :1336-1341
[9]   Selective hydrogen production from methanol oxidative steam reforming over Zn-Cr catalysts with or without Cu loading [J].
Hong, Xuelun ;
Ren, Suzhen .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (02) :700-708
[10]   Production of hydrogen by steam reforming of methanol over copper-based catalysts:: The effect of cesium doping [J].
Houteit, A. ;
Mahzoul, H. ;
Ehrburger, P. ;
Bernhardt, P. ;
Legare, P. ;
Garin, F. .
APPLIED CATALYSIS A-GENERAL, 2006, 306 :22-28