A comparative study of Pt/γ-Al2O3, Au/α-Fe2O3 and CuO-CeO2 catalysts for the selective oxidation of carbon monoxide in excess hydrogen

被引:490
作者
Avgouropoulos, G
Ioannides, T
Papadopoulou, C
Batista, J
Hocevar, S
Matralis, HK
机构
[1] FORTH, Inst Chem Engn & High Temp Chem Proc, GR-26500 Patras, Greece
[2] Univ Patras, Dept Chem, GR-26500 Patras, Greece
[3] Natl Inst Chem, Lab Catalysis & Chem React Engn, SI-1001 Ljubljana, Slovenia
[4] Univ Patras, Dept Chem Engn, GR-26110 Patras, Greece
关键词
carbon monoxide selective oxidation; excess hydrogen; influence of carbon dioxide; influence of water; stability; alumina-supported platinum; gold; iron oxide; copper; ceria;
D O I
10.1016/S0920-5861(02)00058-5
中图分类号
O69 [应用化学];
学科分类号
081704 [应用化学];
摘要
Three different catalysts, namely Pt/gamma-Al2O3, Au/alpha-Fe2O3 and CuO-CeO2 were prepared (by wet impregnation, coprecipitation and a sol-gel method, respectively) and their catalytic performance for the selective oxidation of carbon monoxide in the presence of excess hydrogen was evaluated and compared. The effects of the presence of CO2 and H2O in the reactant feed on the activity and selectivity of these catalysts, as well as their stability under realistic reaction conditions were also investigated. Regardless of whether CO2 or both CO2 and H2O are present in the reactant feed, the Au/alpha-Fe2O3 catalyst is superior to the other two for the selective CO oxidation at relatively low reaction temperatures (<80-120 degreesC, depending on contact time and feed composition employed), while at higher reaction temperatures, best results are obtained with the CuO-CeO2 catalyst, which proved to be more active and remarkably more selective than the Pt/gamma-Al2O3 catalyst. The Au/alpha-Fe2O3 catalyst was the most sensitive, while the Pt/gamma-Al2O3 the most resistant towards deactivation caused by the presence of CO2 and H2O in the feed. Finally, while the Au/alpha-Fe2O3 catalyst lost a considerable portion of its activity during the first 80 h under reaction conditions, the CuO-CeO2 and Pt/gamma-Al2O3 catalysts exhibited a stable catalytic performance, at least during the time period tested in this work (7-8 days). (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:157 / 167
页数:11
相关论文
共 42 条
[1]
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
[2]
Appleby A.J., 1989, FUEL CELL HDB
[3]
CuO-CeO2 mixed oxide catalysts for the selective oxidation of carbon monoxide in excess hydrogen [J].
Avgouropoulos, G ;
Ioannides, T ;
Matralis, HK ;
Batista, J ;
Hocevar, S .
CATALYSIS LETTERS, 2001, 73 (01) :33-40
[4]
Bellows RJ, 1997, ELEC SOC S, V97, P1
[5]
Selective CO oxidation in a hydrogen-rich stream over Au/γ-Al2O3 catalysts [J].
Bethke, GK ;
Kung, HH .
APPLIED CATALYSIS A-GENERAL, 2000, 194 :43-53
[6]
BONACCI JC, 1980, Patent No. 4238468
[7]
PURIFYING HYDROGEN BY ... SELECTIVE OXIDATION OF CARBON MONOXIDE [J].
BROWN, ML ;
GREEN, AW ;
COHN, G ;
ANDERSEN, HC .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1960, 52 (10) :841-844
[8]
A MOLECULAR-BEAM STUDY OF THE CATALYTIC-OXIDATION OF CO ON A PT(111) SURFACE [J].
CAMPBELL, CT ;
ERTL, G ;
KUIPERS, H ;
SEGNER, J .
JOURNAL OF CHEMICAL PHYSICS, 1980, 73 (11) :5862-5873
[9]
COHN JGE, 1965, Patent No. 3216783
[10]
INTERACTIONS BETWEEN OXYGEN AND CARBON-MONOXIDE ON A PD(111) SURFACE [J].
CONRAD, H ;
ERTL, G ;
KUPPERS, J .
SURFACE SCIENCE, 1978, 76 (02) :323-342