Selective formation of alkenes through the cracking of n-heptane on Ca2+-exchanged ferrierite

被引:50
作者
Komatsu, T [1 ]
Ishihara, H [1 ]
Fukui, Y [1 ]
Yashima, T [1 ]
机构
[1] Tokyo Inst Technol, Dept Chem, Meguro Ku, Tokyo 1528550, Japan
关键词
ferrierite; zeolite; cracking; calcium exchange; heptane; alkene selectivity;
D O I
10.1016/S0926-860X(01)00466-5
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 cracking of n-heptane was carried out as a model reaction of naphtha cracking by using various zeolite catalysts to obtain light alkenes. such as ethylene. propylene and butenes. with high selectivity at high conversion levels. The selectivity of zeolites having pore openings of 10 and 12-membered rings was compared at 80% conversion. H-ZSM-5 and H-ferrierite gave higher alkene selectivity than H-MCM-22. H-mordenite. H-beta and H-Y. The effect of exchanged cations on the alkene selectivity was also examined with H-ZSM-5 and H-ferrierite. Ca2+ or Ba2+-exchanged ferrierite gave the highest selectivity to alkenes, 60 C-% at 70%; conversion. The Ca2+-exchange effectively suppressed the secondary hydride transfer that would consume alkenes to form hydrogen-deficient species. As a result, the coke formation from the hydrogen deficient species was also suppressed on Ca2+-exchanged ferrierite. which did not exhibit the rapid deactivation with time-on-stream. (C) 2001 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:103 / 109
页数:7
相关论文
共 21 条
[1]   Monomolecular cracking of n-hexane on Y, MOR, and ZSM-5 zeolites [J].
Babitz, SM ;
Williams, BA ;
Miller, JT ;
Snurr, RQ ;
Haag, WO ;
Kung, HH .
APPLIED CATALYSIS A-GENERAL, 1999, 179 (1-2) :71-86
[2]   THE EFFECTS OF EFAL EXTRACTION ON 2-METHYLPENTANE CRACKING OVER STEAMED HY [J].
BAMWENDA, GR ;
ZHAO, YX ;
GROTEN, WA ;
WOJCIECHOWSKI, BW .
JOURNAL OF CATALYSIS, 1995, 157 (01) :209-221
[3]   CRYSTALLIZATION OF ZEOLITE BETA - EFFECT OF NA AND K-IONS [J].
CAMBLOR, MA ;
PEREZPARIENTE, J .
ZEOLITES, 1991, 11 (03) :202-210
[4]   CATALYTIC CRACKING OF ALKANES ON MCM-22 ZEOLITE - COMPARISON WITH ZSM-5 AND BETA-ZEOLITE AND ITS POSSIBILITY AS AN FCC CRACKING ADDITIVE [J].
CORMA, A ;
GONZALEZALFARO, V ;
ORCHILLES, AV .
APPLIED CATALYSIS A-GENERAL, 1995, 129 (02) :203-215
[5]   SYNTHESIS AND CHARACTERIZATION OF THE MCM-22 ZEOLITE [J].
CORMA, A ;
CORELL, C ;
PEREZPARIENTE, J .
ZEOLITES, 1995, 15 (01) :2-8
[6]   Cracking behavior of zeolites with connected 12- and 10-member ring channels: The influence of pore structure on product distribution [J].
Corma, A ;
Davis, M ;
Fornes, V ;
GonzalezAlfaro, V ;
Lobo, R ;
Orchilles, AV .
JOURNAL OF CATALYSIS, 1997, 167 (02) :438-446
[7]   Hydrogen transfer, coke formation, and catalyst decay and their role in the chain mechanism of catalytic cracking [J].
Cumming, KA ;
Wojciechowski, BW .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1996, 38 (01) :101-157
[8]  
Gates BC, 1979, Chemistry of Catalytic Processes
[9]  
HAAG WO, 1982, FARADAY GENERAL DISC, V72, P317
[10]   Co2+ ion siting in pentasil-containing zeolites II.: Co2+ ion sites and their occupation in ferrierite.: A VIS diffuse reflectance spectroscopy study [J].
Kaucky, D ;
Dedecek, JI ;
Wichterlová, B .
MICROPOROUS AND MESOPOROUS MATERIALS, 1999, 31 (1-2) :75-87