Development of a novel Ru-based catalyst system for the selective oxidation of CO in hydrogen rich gas mixtures

被引:49
作者
Wörner, A [1 ]
Friedrich, C [1 ]
Tamme, R [1 ]
机构
[1] Deutsch Zentrum Luft & Raumfahrt EV, Inst Tech Thermodynam, D-70569 Stuttgart, Germany
关键词
selective oxidation; carbon monoxide; ceramic foam; ruthenium; catalyst; preparation; reforming;
D O I
10.1016/S0926-860X(02)00612-9
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
The hydrogen feedstock for fuel cell applications can be supplied by reforming reactions followed by a water-gas-shift stage, where most of the CO is removed. Still the hydrogen rich gas mixture has to be purified further to prevent the anode's catalyst from severe degradation. At DLR, a novel, technically applicable Ru-based catalyst system was developed for the removal of CO from these gas mixtures by selective oxidation. Reticulated ceramic foams were used as matrix structure. These were coated with gamma-Al2O3 washcoat. Ru was applied as the active metal catalyst by the method of incipient wetness impregnation. Three different precursor materials were investigated. As Ru-nitrosylnitrate turned out to be the most favorable one, the oxidation temperature and the metal loading were varied using this precursor. Both parameters turned out to have a strong influence on catalyst activity and selectivity. The best foam-based catalyst was able to reduce the CO content in a simulated shift exit gas stream containing H-2, CO2, H2O and CO below 30ppm applying an oxygen excess of lambda = 3 in a temperature range between 100 and 160 degreesC, while charging the catalyst with space velocities up to 5000 h(-1). (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:1 / 14
页数:14
相关论文
共 15 条
[1]  
Abele M, 1996, J SOLAR ENERGY ENG, V118, P339
[2]   Combining filtration and catalytic combustion in particulate traps for diesel exhaust treatment [J].
Ambrogio, M ;
Saracco, G ;
Specchia, V .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (04) :1613-1621
[3]  
BIELAWA H, 2000, THESIS RUHR U BOCHUM
[4]   Premixed combustion on ceramic foam burners [J].
Bouma, PH ;
De Goey, LPH .
COMBUSTION AND FLAME, 1999, 119 (1-2) :133-143
[5]   Methane combustion over low-emission catalytic foam burners [J].
Cerri, I ;
Saracco, G ;
Specchia, V .
CATALYSIS TODAY, 2000, 60 (1-2) :21-32
[6]   A carbon monoxide PROX reactor for PEM fuel cell automotive application [J].
Dudfield, CD ;
Chen, R ;
Adcock, PL .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2001, 26 (07) :763-775
[7]   Ceramic foam-supported perovskites as catalysts for combustion of methane [J].
Jiratova, K ;
Moravkova, L ;
Malecha, J ;
Koutsky, B .
COLLECTION OF CZECHOSLOVAK CHEMICAL COMMUNICATIONS, 1997, 62 (06) :875-883
[8]   Radial reactor for trichloroethylene steam reforming [J].
Moates, FC ;
McMinn, TE ;
Richardson, JT .
AICHE JOURNAL, 1999, 45 (11) :2411-2418
[9]   CARBON-MONOXIDE REMOVAL FROM HYDROGEN-RICH FUEL-CELL FEEDSTREAMS BY SELECTIVE CATALYTIC-OXIDATION [J].
OH, SH ;
SINKEVITCH, RM .
JOURNAL OF CATALYSIS, 1993, 142 (01) :254-262
[10]  
Pickenaecker O., 1999, Keram. Z, V51, P108