Support-pore architecture optimization in FCC catalyst particles using designed pore networks

被引:31
作者
El-Nafaty, UA [1 ]
Mann, R [1 ]
机构
[1] Univ Manchester, Inst Sci & Technol, Dept Chem Engn, Manchester M60 1QD, Lancs, England
关键词
catalysis; coke burn-off; 2D stochastic pore networks; catalyst design;
D O I
10.1016/S0009-2509(98)00388-1
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
SEM images of FCC catalyst particles reveal the internal pore space to consist of massive networks of randomly interconnected pores of varying sizes and orientation. Until recently, design of catalyst particles has been restricted mainly to composition, particle size and pore size distribution with little attention paid to pore architecture. With recent advances in computing technology and catalyst characterization techniques it is now possible to move from these 'jumbled' configurations towards more structured controlled pore architectures that could greatly enhance effective utilization of catalyst pore space. In this paper, an application of 2D stochastic networks to investigate the direct influence of pore assembly on diffusion and reaction in FCC catalyst particles is described. Coke burn-off in heavily coked particles was used. Various pore architectural structures were tested including random, positively spiralled, negatively spiralled, structured and interspersed 2D networks. The interspersed network exhibited fastest burn-off kinetics relative to other structures while the random configuration, which probably characterizes most current catalyst particles, showed results better only than the negatively spiralled network. This can be: attributed to enhanced reactant accessibility resulting from absence of transport inefficient micro- and macro-pore clusters and an increase in direct micro-macro pore links characteristic of the designed interspersed network. (C) 1999 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:3475 / 3484
页数:10
相关论文
共 14 条
[1]  
Becker E. R., 1993, COMPUTER AIDED DESIG
[2]   NONUNIFORM DISTRIBUTION OF CATALYSTS ON SUPPORTS .1. BIMOLECULAR LANGMUIR REACTIONS [J].
BECKER, ER ;
WEI, J .
JOURNAL OF CATALYSIS, 1977, 46 (03) :365-371
[3]  
Butt J.B., 1988, Activation, Deactivation, and Poisoning of Catalysts
[4]  
ELNAFATY UA, 1998, THESIS UMIST
[5]  
Hegedus L.L, 1987, CATALYST DESIGN PROG
[6]  
HUGHES R, 1995, CHEM ENG RES DES, V73, P136
[7]  
Mann R, 1996, STUD SURF SCI CATAL, V100, P355
[8]   FLUID CATALYTIC CRACKING - SOME RECENT DEVELOPMENTS IN CATALYST PARTICLE DESIGN AND UNIT HARDWARE [J].
MANN, R .
CATALYSIS TODAY, 1993, 18 (04) :509-528
[9]   OXIDATION OF COKED SILICA-ALUMINA CATALYST [J].
MASSOTH, FE .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1967, 6 (02) :200-&
[10]   Multicomponent diffusion and reaction in three-dimensional networks: General kinetics [J].
Rieckmann, C ;
Keil, FJ .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (08) :3275-3281