Propane as alkylating agent for alkylation of benzene on HZSM-5 and Ga-modified HZSM-5 zeolites

被引:42
作者
Bigey, C [1 ]
Su, BL [1 ]
机构
[1] Univ Namur, Inst Studies Interfaces & Surfaces, Lab Chim Mat Inorgan CMI, B-5000 Namur, Belgium
关键词
benzene alkylation; propane; HZSM-5; Ga-modified HZSM-5; reaction pathways; toluene; ethylbenzene; cumene;
D O I
10.1016/j.molcata.2003.08.023
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
Alkylation of benzene with propane has been studied under continuous-flow condition at atmospheric pressure. Ga-modified HZSM-5 zeolites have shown to be very efficient catalysts for alkylation of benzene with propane. Toluene and ethylbenzene are formed as major products and cumene and n-propylbenzene are also produced at low reaction temperatures in small amounts. The product formation pathways on HZSM-5 and Ga-modified HZSM-5 have been discussed and suggest that acid-catalyzed cracking of propane predominates on HZSM-5, leading to the formation of toluene and ethylbenzene. Over Ga-modified HZSM-5, a bifunctional pathway is noted and cracking of propane and propane dehydrogenation are controlled by Lewis (Gax+)/Bronsted (H+) acid sites ratio. The effect of oxidative and reductive treatments on catalytic activity has been studied and shown that the catalytic activity and the selectivity to toluene of the Ga-modified HZSM-5 zeolite catalysts are enhanced after H-2/O-2 treatment due to the increase in gallium dispersion. (C) 2003 Elsevier B.V. All rights reserved.
引用
收藏
页码:179 / 187
页数:9
相关论文
共 34 条
[1]  
[Anonymous], 1991, [No title captured], Patent No. 0432814
[2]   BENZENE ALKYLATION WITH ETHYLENE AND PROPYLENE OVER H-MORDENITE AS CATALYST [J].
BECKER, KA ;
KARGE, HG ;
STREUBEL, WD .
JOURNAL OF CATALYSIS, 1973, 28 (03) :403-413
[3]   LIQUID-PHASE ALKYLATION OF BENZENE WITH LIGHT OLEFINS CATALYZED BY BETA-ZEOLITES [J].
BELLUSSI, G ;
PAZZUCONI, G ;
PEREGO, C ;
GIROTTI, G ;
TERZONI, G .
JOURNAL OF CATALYSIS, 1995, 157 (01) :227-234
[4]  
BIGEY C, 2000, IND APPL ZEOLITES, P193
[5]  
CHEN J, 1993, P WORLDW SOL AC PROC
[6]   INDUSTRIAL APPLICATION OF SHAPE-SELECTIVE CATALYSIS [J].
CHEN, NY ;
GARWOOD, WE .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1986, 28 (2-3) :185-264
[7]   H.Na-Gallosilicate (MFI) propane aromatization catalyst: Influence of H+ exchange on acidity, activity, and deactivation due to coking [J].
Choudhary, VR ;
Devadas, P ;
Kinage, AK ;
Guisnet, M .
ZEOLITES, 1997, 18 (2-3) :188-195
[8]   Characterization of coke on H-gallosilicate (MFI) propane aromatization catalyst. Influence of coking conditions on nature and removal of coke [J].
Choudhary, VR ;
Sivadinarayana, C ;
Devadas, P ;
Sansare, SD ;
Magnoux, P ;
Guisnet, M .
MICROPOROUS AND MESOPOROUS MATERIALS, 1998, 21 (1-3) :91-101
[9]   Gallium-loaded zeolites for light paraffin aromatization: Evidence for exchanged gallium cation active centers [J].
Dooley, KM ;
Price, GL ;
Kanazirev, VI ;
Hart, VI .
CATALYSIS TODAY, 1996, 31 (3-4) :305-315
[10]   CONVERSION OF LIGHT ALKANES INTO AROMATIC-HYDROCARBONS - 1-DEHYDROCYCLODIMERIZATION OF PROPANE ON PTHZSM-5 CATALYSTS [J].
GNEP, NS ;
DOYEMET, JY ;
SECO, AM ;
RIBEIRO, FR ;
GUISNET, M .
APPLIED CATALYSIS, 1987, 35 (01) :93-108