Propane conversion over a H-ZSM5 acid catalyst - Part 1. Observed kinetics

被引:33
作者
Wang, X
Carabineiro, H
Lemos, F
Lemos, MANDA
Ribeiro, FR
机构
[1] Inst Super Tecn, Ctr Engn Biol & Quim, P-1049001 Lisbon, Portugal
[2] Dalian Univ Technol, Inst Ind Catalysis, Dalian 116012, Peoples R China
关键词
propane; kinetics; zeolite H-ZSM5; catalytic cracking;
D O I
10.1016/j.molcata.2004.02.015
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
This is the first of a series of papers concerning the transformation of propane over a H-ZSM5 catalyst comprising experimental data, a kinetic model, and molecular dynamics calculations. The aim of this work is to provide a more fundamental insight on the catalytic processes involving light alkanes activation over solid acid catalysts. Experimental data for propane cracking was collected in the temperature range 623-773 K and low propane feed partial pressures varying from 3.0 to 9.1 kPa. The results show the existence of two parallel reaction pathways: (1) two monomolecular initiation steps (protolytic cracking or dehydrogenation), characterized by a relatively high activation energy, which becomes predominant at low conversions and high temperatures. Bond rupture may occur on either a C-C or C-H position leading to stoichiometric amounts of methane and ethene, or hydrogen and propene, respectively, when extrapolated at zero conversion; (2) a bimolecular route (classical cracking mechanism) with lower activation energy which involves carbenium ions chain carriers, and whose relative importance grows with increasing conversion and decreasing temperature, as secondary products, mainly olefins, become important. It is also clear that dehydrogenation reactions are favored at low temperatures, while at higher temperatures cracking is the dominant reaction pathway. (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:131 / 137
页数:7
相关论文
共 10 条
[1]   CATALYTIC INVESTIGATION OF THE DEHYDROGENATION PROPERTIES OF PENTASIL TYPE ZEOLITES AS COMPARED WITH THEIR CRACKING PROPERTIES [J].
BANDIERA, J ;
BENTAARIT, Y .
APPLIED CATALYSIS, 1990, 62 (02) :309-316
[2]   Effect of the Bronsted acid site strength on the cracking and dehydrogenating properties in propane conversion - Evidence for the soft-soft/hard-hard acid-base interaction concept [J].
Bandiera, J ;
Dufaux, M ;
BenTaarit, Y .
APPLIED CATALYSIS A-GENERAL, 1997, 148 (02) :283-300
[3]  
HAAG WO, 1984, 8TH P INT C CAT BERL, V2, P305
[4]   13C MAS NMR mechanistic study of propane conversion into butanes over H-MFI catalyst [J].
Ivanova, II ;
Rebrov, AI ;
Pomakhina, EB ;
Derouane, EG .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 1999, 141 (1-3) :107-116
[5]   Solid-acid-catalyzed alkane cracking mechanisms: Evidence from reactions of small probe molecules [J].
Jentoft, FC ;
Gates, BC .
TOPICS IN CATALYSIS, 1997, 4 (1-2) :1-13
[6]   MONOMOLECULAR AND BIOMOLECULAR MECHANISMS OF PARAFFIN CRACKING - N-BUTANE CRACKING CATALYZED BY HZSM-5 [J].
KRANNILA, H ;
HAAG, WO ;
GATES, BC .
JOURNAL OF CATALYSIS, 1992, 135 (01) :115-124
[7]   EFFECT OF GA/PROTON BALANCE IN GA/HZSM-5 CATALYSTS ON C-3 CONVERSION TO AROMATICS [J].
KWAK, BS ;
SACHTLER, WMH .
JOURNAL OF CATALYSIS, 1994, 145 (02) :456-463
[8]   Dehydrogenation of light alkanes over zeolites [J].
Narbeshuber, TF ;
Brait, A ;
Seshan, K ;
Lercher, JA .
JOURNAL OF CATALYSIS, 1997, 172 (01) :127-136
[9]   Monomolecular conversion of light alkanes over H-ZSM-5 [J].
Narbeshuber, TF ;
Vinek, H ;
Lercher, JA .
JOURNAL OF CATALYSIS, 1995, 157 (02) :388-395
[10]   PROPANE CONVERSION ON DRY-AIR-CALCINED HZSM-5 ZEOLITE [J].
RUDHAM, R ;
WINSTANLEY, AW .
JOURNAL OF THE CHEMICAL SOCIETY-FARADAY TRANSACTIONS, 1995, 91 (11) :1689-1694