DEACTIVATION OF CATALYSTS BY COKE FORMATION IN THE PRESENCE OF INTERNAL DIFFUSIONAL LIMITATION

被引：51

作者：

BEECKMAN, JW ^{[1
]}

FROMENT, GF ^{[1
]}

机构：

[1] STATE UNIV GHENT,PETROCHEM TECH LAB,B-9000 GHENT,BELGIUM

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS | 1982年 / 21卷 / 03期

关键词：

D O I：

10.1021/i100007a009

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：243 / 250

页数：8

共 21 条

[1] CATALYST DEACTIVATION BY SITE COVERAGE AND PORE BLOCKAGE - FINITE RATE OF GROWTH OF THE CARBONACEOUS DEPOSIT
BEECKMAN, JW
FROMENT, GF
[J]. CHEMICAL ENGINEERING SCIENCE, 1980, 35 (04) : 805 - 815
[2] CATALYST DEACTIVATION BY ACTIVE-SITE COVERAGE AND PORE BLOCKAGE
BEECKMAN, JW
FROMENT, GF
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1979, 18 (03): : 245 - 256
[3] DEACTIVATION OF POROUS CATALYSTS BY COKE FORMATION
BEECKMANN, JW
FROMENT, GF
PISMEN, L
[J]. CHEMIE INGENIEUR TECHNIK, 1978, 50 (12) : 960 - 961
[4] DEDEKEN JC, 1982, P ISCRE7 M BOSTON
[5] DEACTIVATION OF A PLATINUM REFORMING CATALYST IN A TUBULAR REACTOR
DEPAUW, RP
FROMENT, GF
[J]. CHEMICAL ENGINEERING SCIENCE, 1975, 30 (08) : 789 - 801
[6] NEW NETWORK PERMEABILITY MODEL OF POROUS-MEDIA
DULLIEN, FAL
[J]. AICHE JOURNAL, 1975, 21 (02) : 299 - 307
[7] DEHYDROGENATION OF 1-BUTENE INTO BUTADIENE - KINETICS, CATALYST COKING, AND REACTOR DESIGN
DUMEZ, FJ
FROMENT, GF
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1976, 15 (02): : 291 - 301
[8] PRACTICAL MODELS FOR ISOTHERMAL DIFFUSION AND FLOW OF GASES IN POROUS SOLIDS
FENG, C
STEWART, WE
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1973, 12 (12): : 143 - 147
[9] NON-STEADY STATE BEHAVIOUR OF FIXED BED CATALYTIC REACTORS DUE TO CATALYST FOULING
FROMENT, GF
BISCHOFF, KB
[J]. CHEMICAL ENGINEERING SCIENCE, 1961, 16 (3-4) : 189 - 201
[10] KINETIC DATA AND PRODUCT DISTRIBUTIONS FROM FIXED BED CATALYTIC REACTORS SUBJECT TO CATALYST FOULING
FROMENT, GF
BISCHOFF, KB
[J]. CHEMICAL ENGINEERING SCIENCE, 1962, 17 (02) : 105 - &

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