CONTINUOUS CRYSTALLIZATION OF POTASH ALUM - MSMPR KINETICS

被引:22
|
作者
JONES, AG
MYDLARZ, J
机构
[1] Department of Chemical and Biochemical Engineering, University College London, London, WCIE 7J3, Torrington Place
[2] Institute of Chemical Engineering and Heating Equipment. Technical University of Wroclaw, Wroclaw, 50-373
来源
关键词
crystallization kinetics; drowning‐out precipitation; MSMPR crystallizer; potash alum crystallization;
D O I
10.1002/cjce.5450680210
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The crystallization kinetics of potash alum (aluminium potassium sulphate) from aqueous and aqueous acetone solutions respectively in a continuous mixed‐suspension, mixed‐product‐removal (MSMPR) crystallizer (capacity 4 L) are reported. Growth and nucleation rates are determined by direct model estimation via the population balance analysis of crystal size distribution measured using laser light scattering and sieve analysis. The overall growth rate during drowning‐out precipitation strongly decreases with increasing acetone concentration in the crystallizing solution. Nucleation rates evaluated at zero‐size, however, are virtually unaffected while the “effective” nucleation rates are strongly increased by the presence of acetone with a reduction in the supersaturation order. Magma density dependence is approximately first order during cooling crystallization while a somewhat lower dependence is detected during drowning‐out precipitation. Copyright © 1990 Canadian Society for Chemical Engineering
引用
收藏
页码:250 / 259
页数:10
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