Dispersion of high-viscosity liquid-liquid systems by flow through SMX static mixer elements

被引:27
|
作者
Rao, N. V. Rama [1 ]
Baird, M. H. I. [1 ]
Hrymak, A. N. [1 ]
Wood, P. E. [1 ]
机构
[1] McMaster Univ, Dept Chem Engn, Hamilton, ON L8S 4L7, Canada
关键词
drop; fluid mechanics; multiphase flow; population balance; static mixer;
D O I
10.1016/j.ces.2007.08.070
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The pressure drop and the dispersed phase drop size distribution have been measured for flow through SMX static mixer elements, in columns of diameter 41.18 and 15.75 mm, for a continuous phase of aqueous corn syrup and a dispersed phase of silicone oil. For single-phase flow the pressure drops were consistent with known literature correlations. In the presence of the dispersed phase the pressure drops were increased about 20% above the expected single-phase values, showing more short-term fluctuations but with no significant effect of the flow fraction of the dispersed phase. Droplet size distributions were measured by the computer-aided analysis of images from a digital camera. For shorter lengths of packing the distributions showed a significant "tail" at the large-diameter end, but as the packing length was increased the tail decreased or became non-existent. The mean drop sizes have been compared with a new model based on drop formation at equivalent point sources within the packing. (C) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:6885 / 6896
页数:12
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