Cr2O3 promoted skeletal Cu catalysts for the reactions of methanol steam reforming and water gas shift

被引:56
作者
Ma, L [1 ]
Gong, B
Tran, T
Wainwright, MS
机构
[1] Univ New S Wales, Sch Chem Engn & Ind Chem, Sydney, NSW 2052, Australia
[2] Univ New S Wales, Sch Chem, Sydney, NSW 2052, Australia
基金
澳大利亚研究理事会;
关键词
skeletal copper catalysts; Cr2O3; promoted; methanol steam reforming; water gas shift;
D O I
10.1016/S0920-5861(00)00496-X
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Promotional effects of chromia on the structure and activity of skeletal copper catalysts for methanol steam reforming and water gas shift have been studied. Catalysts were prepared by leaching CuAl2 alloy particles in aqueous NaOH solutions containing sodium chromate at various concentrations. XPS spectra showed that the surface of the resulting catalysts mainly consisted of Cr3+ compounds and Cu-0. Cu+ and/or Cu2+ were not observed by XPS. Increasing the concentration of chromate in the leach liquor resulted in decreases in pore diameter and copper crystallite size but significant enhancement of BET surface area was observed while the total pore volume was maintained. The addition of small amounts of chromate to the leach liquor significantly enhanced the Cu surface area. However, higher concentrations of chromate in the leach liquor decreased the Cu surface areas although the total surface areas increased. The activities of Cr2O3 promoted skeletal copper catalysts for both methanol steam reforming and water gas shift reactions were determined separately. The results indicated that deposition of Cr2O3 On Skeletal copper catalysts significantly improved the specific activities for these reactions. Chromia is found to act as a structural and catalytic promoter for these reactions. (C) 2000 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:499 / 505
页数:7
相关论文
共 26 条
[1]   HYDROGEN-PRODUCTION BY THE CATALYTIC STEAM REFORMING OF METHANOL .1. THE THERMODYNAMICS [J].
AMPHLETT, JC ;
EVANS, MJ ;
JONES, RA ;
MANN, RF ;
WEIR, RD .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1981, 59 (06) :720-727
[2]   HYDROGEN-PRODUCTION BY THE CATALYTIC STEAM REFORMING OF METHANOL .2. KINETICS OF METHANOL DECOMPOSITION USING GIRDLER G66B CATALYST [J].
AMPHLETT, JC ;
EVANS, MJ ;
MANN, RF ;
WEIR, RD .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1985, 63 (04) :605-611
[3]   HYDROGEN-PRODUCTION BY THE CATALYTIC STEAM REFORMING OF METHANOL .3. KINETICS OF METHANOL DECOMPOSITION USING C18HC CATALYST [J].
AMPHLETT, JC ;
MANN, RF ;
WEIR, RD .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1988, 66 (06) :950-956
[4]   METHANOL SYNTHESIS OVER RANEY COPPER-ZINC CATALYSTS .3. OPTIMIZATION OF ALLOY COMPOSITION AND CATALYST PREPARATION [J].
BRIDGEWATER, AJ ;
WAINWRIGHT, MS ;
YOUNG, DJ ;
ORCHARD, JP .
APPLIED CATALYSIS, 1983, 7 (03) :369-382
[5]  
CHARLES E, 1950, Patent No. 2504497
[6]  
Chono M, 1981, SHOKUBAI CATALYST, V23, P3
[7]   PREPARATION AND PROPERTIES OF RANEY COPPER-ZINC CATALYST PELLETS FOR METHANOL SYNTHESIS [J].
CURRYHYDE, HE ;
YOUNG, DJ ;
WAINWRIGHT, MS .
APPLIED CATALYSIS, 1987, 29 (01) :31-41
[8]  
DIXON AG, 1990, P 7 INT SOC EN CONV, P1084
[9]   HYDROGENOLYSIS OF ETHYL FORMATE OVER COPPER-BASED CATALYSTS [J].
EVANS, JW ;
CANT, NW ;
TRIMM, DL ;
WAINWRIGHT, MS .
APPLIED CATALYSIS, 1983, 6 (03) :355-362
[10]   ON THE DETERMINATION OF COPPER SURFACE-AREA BY REACTION WITH NITROUS-OXIDE [J].
EVANS, JW ;
WAINWRIGHT, MS ;
BRIDGEWATER, AJ ;
YOUNG, DJ .
APPLIED CATALYSIS, 1983, 7 (01) :75-83