GAS AND LIQUID HOLD-UP IN 3-PHASE FLUIDIZATION

被引：82

作者：

DARTON, RC ^{[1
]}

HARRISON, D ^{[1
]}

机构：

[1] UNIV CAMBRIDGE,DEPT CHEM ENGN,PEMBROKE ST,CAMBRIDGE CB2 3RA,ENGLAND

来源：

CHEMICAL ENGINEERING SCIENCE | 1975年 / 30卷 / 5-6期

关键词：

D O I：

10.1016/0009-2509(75)80030-3

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：581 / 586

页数：6

共 23 条

[1]

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[2] BED POROSITIES IN GAS-LIQUID FLUIDIZATION [J].

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SUBBARAJ.RV ;

RAO, KV .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1972, 11 (02) :318-+

[3] BED POROSITIES IN GAS-LIQUID FLUIDIZATION [J].

DAKSHINAMURTY, P ;

SUBRAHMA.V ;

RAO, JN .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1971, 10 (03) :322-+

[4]

DARTON RC, 1974, T I CHEM ENG-LOND, V52, P301

[5]

DARTON RC, 1974, MULTI PHASE FLOW SYS, V1

[6]

EFREMOV GI, 1970, INT CHEM ENG, V10, P37

[7] HOLD-UP AND AXIAL MIXING CHARACTERISTICS OF 2 AND 3 PHASE FLUIDIZED-BEDS [J].

KIM, SD ;

BAKER, CGJ ;

BERGOUGNOU, MA .

CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1972, 50 (06) :695-701

[8]

Michelsen M.L., 1970, CHEM ENGNG J, V1, P37

[9]

NICKLIN DJ, 1962, T I CHEM ENGRS, V40, pT61

[10]

OSTEGAARD K, 1968, AICHE IIQPR M TAMPA

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