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：

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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PITT, K
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[2] BROWN DE, 1970, 1970 P CHEM
[3] DROP SIZE DISTRIBUTION IN AGITATED LIQUID-LIQUID SYSTEMS
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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
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RESNICK, W
[J]. AICHE JOURNAL, 1972, 18 (01) : 122 - &
[7] IMPELLER POWER NUMBERS IN CLOSED VESSELS
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MILES, D
[J]. 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