BREAKAGE AND COALESCENCE PROCESSES IN AN AGITATED DISPERSION - EXPERIMENTAL SYSTEM AND DATA REDUCTION

被引：33

作者：

VERHOFF, FH ^{[1
]}

ROSS, SL ^{[1
]}

CURL, RL ^{[1
]}

机构：

[1] UNIV MICHIGAN,DEPT CHEM ENGN,ANN ARBOR,MI 48104

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS | 1977年 / 16卷 / 03期

关键词：

D O I：

10.1021/i160063a012

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：371 / 377

页数：7

共 37 条

[1] A MODEL FOR MASS TRANSFER IN A COALESCING DISPERSION [J].

BAYENS, CA ;

LAURENCE, RL .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1969, 8 (01) :71-&

[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]

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

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

CHEN, HT ;

MIDDLEMA.S .

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

[5] STABILIZING LIQUID-LIQUID DISPERSIONS BY AGITATION [J].

CHURCH, JM ;

SHINNAR, R .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1961, 53 (06) :479-484

[6] DISPERSED PHASE MIXING .1. THEORY AND EFFECTS IN SIMPLE REACTORS [J].

CURL, RL .

AICHE JOURNAL, 1963, 9 (02) :175-181

[7] HYDRODYNAMIC MECHANISM FOR DISINTEGRATION OF SACCHAROMYCES-CEREVESIAE IN AN INDUSTRIAL HOMOGENIZER [J].

DOULAH, MS ;

HAMMOND, TH ;

BROOKMAN, JSG .

BIOTECHNOLOGY AND BIOENGINEERING, 1975, 17 (06) :845-858

[8] COALESCENCE RATES IN A CONTINUOUS-FLOW DISPERSED PHASE SYSTEM [J].

GROOTHUIS, H ;

ZUIDERWEG, FJ .

CHEMICAL ENGINEERING SCIENCE, 1964, 19 (01) :63-66

[9] MEASUREMENT OF COALESCENCE FREQUENCY IN AN AGITATED TANK [J].

HOWARTH, WJ .

AICHE JOURNAL, 1967, 13 (05) :1007-&

[10] RATE OF COALESCENCE OF DISPERSED PHASE IN A LABORATORY MIXER SETTLER UNIT .1. [J].

JEFFREYS, GV ;

DAVIES, GA ;

PITT, K .

AICHE JOURNAL, 1970, 16 (05) :823-&

← 1 2 3 4 →