BUBBLE BREAKAGE IN PIPELINE FLOW

被引:127
作者
HESKETH, RP
ETCHELLS, AW
RUSSELL, TWF
机构
[1] UNIV DELAWARE,DEPT CHEM ENGN,NEWARK,DE 19716
[2] UNIV CAMBRIDGE,DEPT CHEM ENGN,CAMBRIDGE CB2 3RA,ENGLAND
[3] DUPONT CO,NEWARK,DE 19714
关键词
D O I
10.1016/0009-2509(91)80110-K
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The rate of bubble breakage in turbulent liquid flow was examined using a population balance containing a bubble breakage model to analyze experimental bubble breakage rate data. The bubble breakage model was based on high-speed motion photography observations of the breakage process in turbulent liquid pipeline flow. The bubble breakage model predicts the number of bubbles formed from a breakage, the size of the bubbles formed and the rate of bubble breakage. Bubble breakage was determined to be binary; bubble breakage size was described by a breakage size function in which unequal bubble sizes had a higher probability of being formed compared to equal bubble sizes; and the breakage rate was assumed to be first order with respect to the number of bubbles of a given size. The value of the breakage rate constant was found to be approximately equal to the frequency of the second mode of oscillation of the maximum stable bubble size in a given turbulent flow. © 1990.
引用
收藏
页码:1 / 9
页数:9
相关论文
共 21 条
[1]   DROP SIZE DISTRIBUTION OF STIRRED NON-COALESCING LIQUID-LIQUID SYSTEM [J].
BROWN, DE ;
PITT, K .
CHEMICAL ENGINEERING SCIENCE, 1972, 27 (03) :577-&
[2]   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
[3]   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
[4]   DROP-SIZE DISTRIBUTIONS PRODUCED BY TURBULENT PIPE FLOW OF IMMISCIBLE LIQUIDS [J].
COLLINS, SB ;
KNUDSEN, JG .
AICHE JOURNAL, 1970, 16 (06) :1072-&
[5]   DESCRIPTION OF INTERACTION PROCESSES IN AGITATED LIQUID-LIQUID DISPERSIONS [J].
COULALOGLOU, CA ;
TAVLARIDES, LL .
CHEMICAL ENGINEERING SCIENCE, 1977, 32 (11) :1289-1297
[6]   MODEL FOR BREAKUP RATE OF SPHERICAL DROPS IN ISOTROPIC TURBULENT FLOWS [J].
DELICHATSIOS, MA .
PHYSICS OF FLUIDS, 1975, 18 (06) :622-623
[7]   EFFECT OF COALESCENCE ON AVERAGE DROP SIZE IN LIQUID-LIQUID DISPERSIONS [J].
DELICHATSIOS, MA ;
PROBSTEIN, RF .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1976, 15 (02) :134-138
[8]   BUBBLE-SIZE IN HORIZONTAL PIPELINES [J].
HESKETH, RP ;
RUSSELL, TWF ;
ETCHELLS, AW .
AICHE JOURNAL, 1987, 33 (04) :663-667
[9]  
HESKETH RP, 1987, THESIS U DELAWARE
[10]  
HESKETH RP, 1990, UNPUB IND ENG CHEM R