The methanol-to-olefins conversion over zeolite-coated ceramic foams

被引:93
作者
Patcas, FC [1 ]
机构
[1] Univ Karlsruhe, Inst Chem Proc Engn, CVT, D-76128 Karlsruhe, Germany
关键词
MTO; methanol conversion; olefin; hydrocarbon pool; ceramic foam; ZSM-5; zeolite washcoat; structured packing; propylene;
D O I
10.1016/j.jcat.2005.01.016
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 use of ZSM-5-coated ceramic foam packing in the conversion of methanol to olefins showed substantial activity and selectivity improvements as compared with conventional extruded zeolite pellets. The formation of propylene was particularly favored over the coated foams. At 380 degrees C the amount of ethylene and propylene produced per unit volume of reactor packing was 2.5 times higher over the zeolite-coated foams than over pellets. However, at a lower temperature (320 degrees C) and higher space velocities the zeolite-coated foams were less active than the zeolite pellets. This behavior could be explained by the autocatalytic hydrocarbon pool mechanism. The species involved in the autocatalytic process, which are in equilibrium with the products, were decomposed and flushed off when the space velocity was high or the characteristic size of the catalyst bulk was too small. Thus the zeolite coat has to be optimized to ensure simultaneously a high effectiveness factor and sufficient buildup of catalytic species. (c) 2005 Elsevier Inc. All rights reserved.
引用
收藏
页码:194 / 200
页数:7
相关论文
共 19 条
[11]  
Froment GF, 1992, CATALYSIS, V9, P1, DOI DOI 10.1039/9781847553218-00001
[12]  
GREEN DW, 1998, PERRYS CHEM ENG HDB, pCH5
[13]  
LEVENSPIEL O, 1999, CHEM REACTION ENG, P388
[14]   KINETIC-MODEL FOR METHANOL CONVERSION TO OLEFINS [J].
MIHALL, R ;
STRAJA, S ;
MARIA, G ;
MUSCA, G ;
POP, G .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1983, 22 (03) :532-538
[15]   FORMATION OF ETHENE AND PROPENE FROM METHANOL ON ZEOLITE ZSM-5 .1. INVESTIGATION OF RATE AND SELECTIVITY IN A BATCH REACTOR [J].
PRINZ, D ;
RIEKERT, L .
APPLIED CATALYSIS, 1988, 37 (1-2) :139-154
[16]   KINETIC REGIMES OF ZEOLITE DEACTIVATION AND REANIMATION [J].
SCHULZ, H ;
LAU, K ;
CLAEYS, M .
APPLIED CATALYSIS A-GENERAL, 1995, 132 (01) :29-40
[17]   Direct evidence for a catalytically active role of the hydrocarbon pool formed on zeolite H-ZSM-5 during the methanol-to-olefin conversion [J].
Seiler, M ;
Wang, W ;
Buchholz, A ;
Hunger, M .
CATALYSIS LETTERS, 2003, 88 (3-4) :187-191
[18]   Supramolecular origins of product selectivity for methanol-to-olefin catalysis on HSAPO-34 [J].
Song, WG ;
Fu, H ;
Haw, JF .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 2001, 123 (20) :4749-4754
[19]   Methanol-to-hydrocarbons:: catalytic materials and their behavior [J].
Stöcker, M .
MICROPOROUS AND MESOPOROUS MATERIALS, 1999, 29 (1-2) :3-48