Selective oxidation of CO in excess hydrogen over CuO/CexSn1-xO2 catalysts

被引:66
作者
Chen, YZ [1 ]
Liaw, BJ
Huang, CW
机构
[1] Natl Cent Univ, Dept Chem & Mat Engn, Jhongli 32048, Taiwan
[2] Nanya Inst Technol, Dept Chem Engn, Jhongli 32091, Taiwan
关键词
selective CO oxidation; CuO catalyst; CeO2; oxide; Ce-Sn-O mixed oxides;
D O I
10.1016/j.apcata.2005.12.032
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
CexSn1-xO2(1-x = 0.1-0.5) mixed oxides were prepared as supports of CuO/CexSn1-xO2 catalysts. They were characterized and used in the selective oxidation of CO in excess hydrogen. Incorporating Sn4+ into CeO2 not only increased the mobility of lattice oxygen but also promoted the activity of the selective CO oxidation. These promoting effects were attributed to the redox behaviors of Ce4+/Ce3+ and Sn4+/Sn2+ in CexSn1-xO2 mixed oxides and to the interfacial interaction between fine clusters of CuO and CexSn1-xO2. Of these CuO/Ce(x)Sn(1-x)O2 catalysts, 7% CuO/ Ce0.9Sn0.1O2 catalyst was the most active one; it was and more active than the 7% CuO/CeO2 catalyst, with a T-100 temperature (80-85 degrees C) for complete conversion that was about 15 degrees C less than that of 7% CuO/CeO2 (95-100 degrees C). The selective oxidation of CO was still promoted as the incorporated amount of Sn4+ exceeded 10%, which is different from the result of incorporating Zr4+ in CexZr1-xO2 (1 - x > 0.1). Such incorporation of Zr4+ in CexZr1-xO2 weakened the selective oxidation. The 7% CuO/Ce0.9Sn0.1O2 catalyst was almost inactive in H-2 oxidation below 110 degrees C, and it achieved a selectivity of approximately 100%. The activity of the 7% CuO/Ce0.9Sn0.1O2 catalyst was weakened in the feed in the presence of CO2 and H2O, but the stability of the catalyst was maintained. The 7% CuO/Ce0.9Sn0.1O2 catalyst exhibited a good activity that was comparable with that of the noble metal catalyst of 5% Pt/Al2O3 and a good selectivity of much greater than 5% Pt/Al2O3. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:168 / 176
页数:9
相关论文
共 39 条
[21]  
Lin R, 2001, INDIAN J CHEM A, V40, P36
[22]   TOTAL OXIDATION OF CARBON-MONOXIDE AND METHANE OVER TRANSITION METAL-FLUORITE OXIDE COMPOSITE CATALYSTS .2. CATALYST CHARACTERIZATION AND REACTION-KINETICS [J].
LIU, W ;
FLYTZANI-STEPHANOPOULOS, M .
JOURNAL OF CATALYSIS, 1995, 153 (02) :317-332
[23]   TPR and TPD studies of CuO/CeO2 catalysts for low temperature CO oxidation [J].
Luo, MF ;
Zhong, YJ ;
Yuan, XX ;
Zheng, XM .
APPLIED CATALYSIS A-GENERAL, 1997, 162 (1-2) :121-131
[24]   Selective CO oxidation over Pt/alumina catalysts for fuel cell applications [J].
Manasilp, A ;
Gulari, E .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2002, 37 (01) :17-25
[25]   Comparative study on redox properties and catalytic behavior for CO oxidation of CuO/CeO2 and CuO/ZrCeO4 catalysts [J].
Martínez-Arias, A ;
Fernández-García, M ;
Gálvez, O ;
Coronado, JM ;
Anderson, JA ;
Conesa, JC ;
Soria, J ;
Munuera, G .
JOURNAL OF CATALYSIS, 2000, 195 (01) :207-216
[26]   Study of the redox behaviour of high surface area CeO2-SnO2 solid solutions [J].
Nguyen, TB ;
Deloume, JP ;
Perrichon, V .
APPLIED CATALYSIS A-GENERAL, 2003, 249 (02) :273-284
[27]   Ceria films on zirconia substrates: models for understanding oxygen-storage properties [J].
Putna, ES ;
Bunluesin, T ;
Fan, XL ;
Gorte, RJ ;
Vohs, JM ;
Lakis, RE ;
Egami, T .
CATALYSIS TODAY, 1999, 50 (02) :343-352
[28]   Large-scale hydrogen production [J].
Rostrup-Nielsen, JR ;
Rostrup-Nielsen, T .
CATTECH, 2002, 6 (04) :150-159
[29]  
Sanchez RMT, 1997, J CATAL, V168, P125
[30]   KINETICS OF CATALYTIC STEAM REFORMING OF METHANOL IN A CSTR REACTOR [J].
SANTACESARIA, E ;
CARRA, S .
APPLIED CATALYSIS, 1983, 5 (03) :345-358