EFFECT OF IMPELLER GEOMETRY ON DROP BREAK-UP IN A STIRRED LIQUID-LIQUID CONTRACTOR

被引：42

作者：

BROWN, DE ^{[1
]}

PITT, K ^{[1
]}

机构：

[1] UNIV MANCHESTER,INST SCI & TECHNOL,DEPT CHEM ENGN,MANCHESTER,ENGLAND

来源：

CHEMICAL ENGINEERING SCIENCE | 1974年 / 29卷 / 02期

关键词：

D O I：

10.1016/0009-2509(74)80042-4

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：345 / 348

页数：4

共 17 条

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[2]

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

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MIDDLEMA.S .

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[4]

Danckwerts PV, 1952, CHEM ENG SCI, V2, P1

[5]

HOLMES DB, 1964, CHEM ENG SCI, V19, P209

[6] DROP SIZES IN AN AGITATED LIQUID-LIQUID SYSTEM [J].

MLYNEK, Y ;

RESNICK, W .

AICHE JOURNAL, 1972, 18 (01) :122-&

[7] IMPELLER POWER NUMBERS IN CLOSED VESSELS [J].

NIENOW, AW ;

MILES, D .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1971, 10 (01) :41-&

[8]

OLDSHUE JY, 1969, P BIOCHEM, V4, P51

[9]

PITT K, 1968, THESIS U MANCHESTER

[10]

PROCHAZKA J, 1961, COLLECT CZECH CHEM C, V26, P2961

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