A MODEL FOR MASS TRANSFER IN A COALESCING DISPERSION

被引:20
作者
BAYENS, CA
LAURENCE, RL
机构
[1] Department of Chemical Engineering, Johns Hopkins University, Baltimore, Md.
[2] Department of Chemical Engineering, University of Massachusetts, Amherst
来源
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS | 1969年 / 8卷 / 01期
关键词
D O I
10.1021/i160029a012
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Mass transfer between the two phases of a liquid-liquid dispersion is affected by drop coalescence and breakup. When all the droplets have the same residence time, a proper description of the drop population requires a trivariate distribution function. The distribution, dependent on the residence time of the dispersion, is written in terms of the size of a drop, amount of solute in a drop, and drop age. Population balances for a homogeneous, batch stirred tank and a steady-state, laminar flow spray column are developed. These equations are solved for the average solute concentration in the dispersed phase as a function of two dimensionless groups: where D is a diffusion coefficient, Θ a residence time, the initial average drop size, and ωi a drop interaction frequency. © 1969, American Chemical Society. All rights reserved.
引用
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页码:71 / &
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