A PHYSICAL INTERPRETATION OF DROP SIZES IN HOMOGENIZERS AND AGITATED TANKS, INCLUDING THE DISPERSION OF VISCOUS OILS

被引:129
作者
DAVIES, JT
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10.1016/0009-2509(87)80172-0
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TQ [化学工业];
学科分类号
0817 ;
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页码:1671 / 1676
页数:6
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共 22 条
[1]  
BERKMAN PD, 1985, 1985 AICHE ANN M CHI
[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, P83
[4]   DROP BREAKUP IN TURBULENT STIRRED-TANK CONTACTORS .1. EFFECT OF DISPERSED-PHASE VISCOSITY [J].
CALABRESE, RV ;
CHANG, TPK ;
DANG, PT .
AICHE JOURNAL, 1986, 32 (04) :657-666
[5]   DROP BREAKUP IN TURBULENT STIRRED-TANK CONTACTORS .3. CORRELATIONS FOR MEAN SIZE AND DROP SIZE DISTRIBUTION [J].
CALABRESE, RV ;
WANG, CY ;
BRYNER, NP .
AICHE JOURNAL, 1986, 32 (04) :677-681
[6]  
CALABRESE RV, 1986, COMMUNICATION
[7]   FLOW AND TURBULENCE IN A STIRRED TANK [J].
CUTTER, LA .
AICHE JOURNAL, 1966, 12 (01) :35-&
[8]  
Davies J. T., 1972, TURBULENCE PHENOMENA
[9]   DROP SIZES OF EMULSIONS RELATED TO TURBULENT ENERGY-DISSIPATION RATES [J].
DAVIES, JT .
CHEMICAL ENGINEERING SCIENCE, 1985, 40 (05) :839-842
[10]  
DAVIES JT, 1986, THESIS U BIRMINGHAM