LIQUID-LIQUID INTERFACIAL-AREAS FORMED BY TURBINE IMPELLERS IN BAFFLED, CYLINDRICAL MIXING TANKS

被引：32

作者：

ECKERT, RE

MCLAUGHLIN, CM

RUSHTON, JH

机构：

[1] Purdue Univ, Sch of Chemical, Engineering, West Lafayette, IN, USA, Purdue Univ, Sch of Chemical Engineering, West Lafayette, IN, USA

来源：

AICHE JOURNAL | 1985年 / 31卷 / 11期

关键词：

D O I：

10.1002/aic.690311107

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

MIXING

引用

页码：1811 / 1820

页数：10

共 36 条

[1]

Bouyatiotis B., 1967, I CHEM ENG S SER, P43

[2] EFFECT OF IMPELLER GEOMETRY ON DROP BREAK-UP IN A STIRRED LIQUID-LIQUID CONTRACTOR [J].

BROWN, DE ;

PITT, K .

CHEMICAL ENGINEERING SCIENCE, 1974, 29 (02) :345-348

[3]

BROWN DE, 1970, P CHEMECA 70 MELBOUR, V83

[4]

Calderbank P., 1958, TRANS INST CHEM ENG, V36, P443

[5] DROP SIZE DISTRIBUTION IN AGITATED LIQUID-LIQUID SYSTEMS [J].

CHEN, HT ;

MIDDLEMA.S .

AICHE JOURNAL, 1967, 13 (05) :989-+

[6] DROP SIZE DISTRIBUTIONS AND COALESCENCE FREQUENCIES OF LIQUID-LIQUID DISPERSIONS IN FLOW VESSELS [J].

COULALOGLOU, CA ;

TAVLARIDES, LL .

AICHE JOURNAL, 1976, 22 (02) :289-297

[7]

DAVIES OL, 1963, DESIGN ANAL IND EXPT, P532

[8] EFFECTIVE INTERFACIAL AREA IN AGITATED LIQUID-LIQUID CONTACTORS [J].

FERNANDE.JB ;

SHARMA, MM .

CHEMICAL ENGINEERING SCIENCE, 1967, 22 (10) :1267-&

[9]

HILLESTAD JG, 1965, THESIS PURDUE U LAFA

[10]

KAFAROV VV, 1959, J APPL CHEM-USSR, V32, P810

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