H2 reduction behaviors and catalytic performance of bimetallic tin-modified platinum catalysts for propane dehydrogenation

被引:101
作者
Salmones, J
Wang, JA
Galicia, JA
Aguilar-Rios, G
机构
[1] Inst Mexicano Petr, Programa Tratamiento Crudo Maya, Mexico City 07730, DF, Mexico
[2] Inst Politecn Nacl, Escuela Super Ingn Quim & Ind Extractivas, UPALM, Mexico City 07738, DF, Mexico
关键词
propane dehydrogenation; Pt-Sn/MgAl2O4; catalysts; tin effects; TPR; catalytic stability; acidity;
D O I
10.1016/S1381-1169(01)00525-8
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
Bimetallic Pt-Sn/MgAl2O4 catalysts with different metal concentrations, used for propane dehydrogenation, were prepared by the impregnation, coprecipitation-impregnation and sol-gel methods. Pore size distribution and surface acidity of the catalysts were studied by N-2 physisorption and temperature programmed desorption of ammonia (TPD-NH3), respectively. Reduction behaviors of the catalysts were characterized by temperature programmed reduction (TPR) technique. In the catalysts containing 0.6 wt.% Sn, some platinum-modified by tin crystals were produced by association with acid sites of the support, where hydrogen reduction took place above 500degreesC. These tin-modified platinum species were found to be favorable for propane dehydrogenation reaction and also to be responsible for the improvement of the activity as tin content increases from 0.3 to 0.6 wt.%. Metal dispersion, pore size distribution and acidity of the support strongly impact the selectivity and stability of the catalysts. The sol-gel catalyst showed better selectivity but lower stability compared to other catalysts that can be explained by its very narrow pore size distribution and relatively stronger acidity as well as more homogeneous metal distribution on the support. When the catalysts were pretreated with oxygen and then hydrogen, their catalytic activities were significantly enhanced largely due to a better metal distribution on the support. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:203 / 213
页数:11
相关论文
共 25 条
[1]   Propane dehydrogenation activity of Pt and Pt-Sn catalysts supported on magnesium aluminate:: influence of steam and hydrogen [J].
Aguilar-Ríos, G ;
Salas, P ;
Valenzuela, MA ;
Armendáriz, H ;
Wang, JA ;
Salmones, J .
CATALYSIS LETTERS, 1999, 60 (1-2) :21-25
[2]   HYDROGEN INTERACTIONS AND CATALYTIC PROPERTIES OF PLATINUM-TIN SUPPORTED ON ZINC ALUMINATE [J].
AGUILARRIOS, G ;
VALENZUELA, M ;
SALAS, P ;
ARMENDARIZ, H ;
BOSCH, P ;
DELTORO, G ;
SILVA, R ;
BERTIN, V ;
CASTILLO, S ;
RAMIREZSOLIS, A ;
SCHIFTER, I .
APPLIED CATALYSIS A-GENERAL, 1995, 127 (1-2) :65-75
[3]   Influence of oxychlorination treatment on the surface and bulk properties of a Pt-Sn/Al2O3 catalyst [J].
Arteaga, GJ ;
Anderson, JA ;
Becker, SM ;
Rochester, CH .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 1999, 145 (1-2) :183-201
[4]   Propane dehydrogenation over supported Pt and Pt-Sn catalysts: Catalyst preparation, characterization, and activity measurements [J].
Barias, OA ;
Holmen, A ;
Blekkan, EA .
JOURNAL OF CATALYSIS, 1996, 158 (01) :1-12
[5]   CONVERSION OF METHYLCYCLOPENTANE ON PLATINUM-TIN REFORMING CATALYSTS [J].
COQ, B ;
FIGUERAS, F .
JOURNAL OF CATALYSIS, 1984, 85 (01) :197-205
[6]   Effects of potassium on silica-supported Pt and Pt/Sn catalysts for isobutane dehydrogenation [J].
Cortright, RD ;
Dumesic, JA .
JOURNAL OF CATALYSIS, 1995, 157 (02) :576-583
[7]   MICROCALORIMETRIC, SPECTROSCOPIC, AND KINETIC-STUDIES OF SILICA-SUPPORTED PT AND PT/SN CATALYSTS FOR ISOBUTANE DEHYDROGENATION [J].
CORTRIGHT, RD ;
DUMESIC, JA .
JOURNAL OF CATALYSIS, 1994, 148 (02) :771-778
[8]   CONVERSION OF N-HEXANE OVER MONO-FUNCTIONAL SUPPORTED AND UNSUPPORTED PTSN CATALYSTS [J].
DAUTZENBERG, FM ;
HELLE, JN ;
BILOEN, P ;
SACHTLER, WMH .
JOURNAL OF CATALYSIS, 1980, 63 (01) :119-128
[9]  
Evans G.R., 1995, ERDOL ERDGAS KOHLE, V111, P271
[10]  
FAN YI, 1991, STUD SURF SCI CATAL, V68, P683