SIMULATION OF AN ADIABATIC PACKED-BED REACTOR

被引：31

作者：

KARANTH, NG ^{[1
]}

HUGHES, R ^{[1
]}

机构：

[1] UNIV SALFORD,DEPT CHEM ENGN,SALFORD,LANCASHIRE,ENGLAND

来源：

CHEMICAL ENGINEERING SCIENCE | 1974年 / 29卷 / 01期

关键词：

D O I：

10.1016/0009-2509(74)85045-1

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

收藏

页码：197 / 205

页数：9

相关论文

共 20 条

[1] Barkelew C.H., 1959, CHEM ENG PROG S SER, P25
[2] A COMPUTER MODEL OF THE FIXED BED CATALYTIC REACTOR - THE ADIABATIC AND QUASI-ADIABATIC CASES
CARBERRY, JJ
WENDEL, MM
[J]. AICHE JOURNAL, 1963, 9 (01) : 129 - 133
[3] CONTINUOUS FLOW SYSTEMS - DISTRIBUTION OF RESIDENCE TIMES
DANCKWERTS, PV
[J]. CHEMICAL ENGINEERING SCIENCE, 1953, 2 (01) : 1 - 13
[4] A COMPUTATIONAL MODEL FOR PREDICTING AND CORRELATING THE BEHAVIOR OF FIXED-BED REACTORS .1. DERIVATION OF MODEL FOR NONREACTIVE SYSTEMS
DEANS, HA
LAPIDUS, L
[J]. AICHE JOURNAL, 1960, 6 (04) : 656 - 663
[5] FAN LT, 1971, CHEM ENG SCI, V26, P379
[6] MATHEMATICAL MODELS FOR TRANSIENT BEHAVIOR OF A PACKED BED REACTOR
FEICK, J
QUON, D
[J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1970, 48 (02) : 205 - &
[7] Ferguson N. B., 1970, CHEM ENG J, V1, P327, DOI [10.1016/0300-9467(70)85021-3, DOI 10.1016/0300-9467(70)85021-3]
[8] PACKED BED REACTOR ANALYSIS BY ORTHOGONAL COLLOCATION
FINLAYSON, BA
[J]. CHEMICAL ENGINEERING SCIENCE, 1971, 26 (07) : 1081 - +
[9] INFLUENCE OF CATALYST PARTICLE SIZE ON REACTION KINETICS - HYDROGENATION OF ETHYLENE ON NICKEL
FULTON, JW
CROSSER, OK
[J]. AICHE JOURNAL, 1965, 11 (03) : 513 - +
[10] Gunn D, 1968, CHEM ENG J, V219, pCE153