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

页码：197 / 205

页数：9

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 [J].

CARBERRY, JJ ;

WENDEL, MM .

AICHE JOURNAL, 1963, 9 (01) :129-133

[3] CONTINUOUS FLOW SYSTEMS - DISTRIBUTION OF RESIDENCE TIMES [J].

DANCKWERTS, PV .

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 [J].

DEANS, HA ;

LAPIDUS, L .

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 [J].

FEICK, J ;

QUON, D .

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 [J].

FINLAYSON, BA .

CHEMICAL ENGINEERING SCIENCE, 1971, 26 (07) :1081-+

[9] INFLUENCE OF CATALYST PARTICLE SIZE ON REACTION KINETICS - HYDROGENATION OF ETHYLENE ON NICKEL [J].

FULTON, JW ;

CROSSER, OK .

AICHE JOURNAL, 1965, 11 (03) :513-+

[10]

Gunn D, 1968, CHEM ENG J, V219, pCE153

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