Deep oxidation of propane on Pt-supported catalysts:: drastic turnover rate enhancement using zeolite supports

被引:140
作者
Garetto, TF [1 ]
Rincón, E [1 ]
Apesteguía, CR [1 ]
机构
[1] UNL, CONICET, INCAPE, Inst Invest Catalisis & Petroquim, RA-3000 Santa Fe, Argentina
关键词
propane combustion; Pt catalysts; acid zeolites;
D O I
10.1016/j.apcatb.2003.10.004
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 combustion of propane was studied on Pt supported on MgO, alumina, and zeolites KL, HY, ZSM5 and Beta. Samples contained a similar amount of Pt, between 0.32 and 0.44%, and were characterized by employing a variety of physical and spectroscopic techniques. The catalyst activities were evaluated through both conversion versus temperature (light-off curves) and conversion versus time catalytic tests. Kinetic studies showed that the reaction is first order in propane, and zero (Pt/Al2O3, Pt/MgO) or negative (Pt/zeolites) orders in oxygen. Apparent activation energies (E-a) and pre-exponential factors (A) were determined and it was verified that the experimental data obey a Constable relation (In A = mE(a) + c). Pt/Al2O3 catalysts of different metallic dispersions were prepared for investigating the effect of Pt crystallite size on combustion activity. It was found that propane oxidation is a structure insensitive reaction on Pt/AL(2)O(3). Propane oxidation turnover rates (TOF) followed the order: Pt/MgO < Pt/Al2O3 much less than Pt/KL < Pt/HY less than or equal to Pt/ZSM5 < Pt/Beta. The TOF values on Pt/acid zeolites were more than two orders of magnitude higher than on Pt/Al2O3. Propane oxidation activity was also significantly higher on Pt/KL as compared to Pt/Al2O3, despite that Al2O3 and zeolite KL supports exhibited similar acid sites density and strength. This result showed that the support acid strength did not have a major influence on propane combustion activity. Areal propane uptake was more than one order of magnitude higher on Pt/zeolites than on Pt/Al2O3 and this drastic increase in the density of propane adsorbed species may promote the alkane oxidation rate. It is proposed that the enhanced combustion activity obtained on Pt/zeolites is associated with an additional oxidation pathway from propane adsorbing on the metal-oxide interface region and reacting with oxygen spilled-over from the metal surface. (C) 2003 Elsevier B.V. All rights reserved.
引用
收藏
页码:167 / 174
页数:8
相关论文
共 27 条
[1]   Kinetic study of the catalytic oxidation of alkanes over nickel, palladium, and platinum foils [J].
Aryafar, M ;
Zaera, F .
CATALYSIS LETTERS, 1997, 48 (3-4) :173-183
[2]   Compensation phenomena in heterogeneous catalysis: General principles and a possible explanation [J].
Bond, GC ;
Keane, MA ;
Kral, H ;
Lercher, JA .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 2000, 42 (03) :323-383
[3]   The nature of activity enhancement for propane oxidation over supported Pt catalysts exposed to sulphur dioxide [J].
Burch, R ;
Halpin, E ;
Hayes, M ;
Ruth, K ;
Sullivan, JA .
APPLIED CATALYSIS B-ENVIRONMENTAL, 1998, 19 (3-4) :199-207
[4]   Kinetics and mechanism of the reduction of NO by C3H8 over Pt/Al2O3 under lean-burn conditions [J].
Burch, R ;
Watling, TC .
JOURNAL OF CATALYSIS, 1997, 169 (01) :45-54
[5]   REMOVAL AND DESTRUCTION OF BENZENE, TOLUENE, AND XYLENE FROM WASTE-WATER BY AIR STRIPPING AND CATALYTIC-OXIDATION [J].
CHUANG, KT ;
CHENG, S ;
TONG, SM .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1992, 31 (11) :2466-2472
[7]  
Cremer E, 1929, Z PHYS CHEM A-CHEM T, V144, P231
[8]   Base catalysis for the synthesis of alpha,beta-unsaturated ketones from the vapor-phase aldol condensation of acetone [J].
DiCosimo, JI ;
Diez, VK ;
Apesteguia, CR .
APPLIED CATALYSIS A-GENERAL, 1996, 137 (01) :149-166
[9]   Structure sensitivity and in situ activation of benzene combustion on Pt/Al2O3 catalysts [J].
Garetto, TF ;
Apesteguía, CR .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2001, 32 (1-2) :83-94
[10]   Oxidative catalytic removal of hydrocarbons over Pt/Al2O3 catalysts [J].
Garetto, TF ;
Apesteguía, CR .
CATALYSIS TODAY, 2000, 62 (2-3) :189-199