Axial Dispersion in a Pulsed and Nonpulsed Disc and Doughnut Solvent Extraction Column

被引:14
|
作者
Wang, Yong [1 ]
Yi, Heng [2 ]
Smith, Kathryn H. [1 ]
Mumford, Kathryn A. [1 ]
Stevens, Geoffrey W. [1 ]
机构
[1] Univ Melbourne, Dept Chem & Biomol Engn, Particulate Fluids Proc Ctr, Parkville, Vic 3010, Australia
[2] Tsinghua Univ, Dept Chem Engn, Beijing 100084, Peoples R China
基金
澳大利亚研究理事会;
关键词
MASS-TRANSFER; PLATE; PREDICTION; COEFFICIENTS; SIMULATIONS; PERFORMANCE;
D O I
10.1021/acs.iecr.6b04353
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In solvent extraction columns mechanical agitation is usually introduced to improve the extraction efficiency. However, some industrial columns have been found to have higher extraction efficiency while running with no pulsation. In this study, axial dispersion coefficients in the continuous phase were measured under pulsing and nonpulsing conditions using a 72.5 mm diameter disc and doughnut solvent extraction column. The axial dispersion coefficients were measured using the unsteady tracer injection method. Under nonpulsing conditions, the axial dispersion coefficient increased with increasing continuous phase velocity, but it did not change significantly with the increase of the dispersed phase velocity. With increasing pulsation intensity, the axial dispersion coefficient increased. A correlation is proposed to predict the continuous phase axial dispersion coefficient in a pulsing and nonpulsing disc and doughnut solvent extraction column.
引用
收藏
页码:4052 / 4059
页数:8
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