Modeling of catalyst deactivation

被引:107
作者
Froment, GF [1 ]
机构
[1] Texas A&M Univ, Dept Chem Engn, College Stn, TX 77843 USA
关键词
catalyst deactivation; percolation theory; pore network; pore blockage;
D O I
10.1016/S0926-860X(00)00850-4
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
Coke formation and its effect on the catalyst is modeled at three levels: the active site, the particle, and the reactor. At the site level, information on the chemical pathways leading to the deactivating agent and on its interaction with the sites is essential. At the particle level, the presence of concentration profiles and the influence of the structure of the pore network have to be accounted for. The latter aspect is dealt with through percolation theory and the effective medium approximation. At the reactor level, the non-steady-state behavior caused by the deactivation of the catalyst is illustrated. The parallelism between the modeling of deactivation by coke formation and a specific type of poisoning leading to pore blockage is briefly discussed. (C) 2001 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:117 / 128
页数:12
相关论文
共 27 条
[1]  
[Anonymous], 2018, INTRO PERCOLATION TH
[2]   CATALYST DEACTIVATION BY ACTIVE-SITE COVERAGE AND PORE BLOCKAGE [J].
BEECKMAN, JW ;
FROMENT, GF .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1979, 18 (03) :245-256
[3]  
Beeckman JW, 1999, STUD SURF SCI CATAL, V126, P17
[4]   A PERCOLATION APPROACH FOR THE MODELING OF DEACTIVATION OF ZEOLITE CATALYSTS BY COKE FORMATION [J].
BEYNE, AOE ;
FROMENT, GF .
CHEMICAL ENGINEERING SCIENCE, 1990, 45 (08) :2089-2096
[5]   A PERCOLATION APPROACH FOR THE MODELING OF DEACTIVATION OF ZEOLITE CATALYSTS BY COKE FORMATION - DIFFUSIONAL LIMITATIONS AND FINITE RATE OF COKE GROWTH [J].
BEYNE, AOE ;
FROMENT, GF .
CHEMICAL ENGINEERING SCIENCE, 1993, 48 (03) :503-511
[6]  
Butt J.B., 1988, Activation, Deactivation, and Poisoning of Catalysts
[7]  
Butt JB, 1997, STUD SURF SCI CATAL, V111, P69
[8]  
Delmon B, 1997, STUD SURF SCI CATAL, V111, P39
[9]   DEHYDROGENATION OF 1-BUTENE INTO BUTADIENE - KINETICS, CATALYST COKING, AND REACTOR DESIGN [J].
DUMEZ, FJ ;
FROMENT, GF .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1976, 15 (02) :291-301
[10]  
Froment G.F., 1980, CATALYST DEACTIVATIO, V6, P1