A state-of-the-art review on single drop study in liquid-liquid extraction: Experiments and simulations

被引:27
作者
Zhang, Jiyizhe [1 ]
Wang, Yundong [1 ]
Stevens, Geoffrey W. [2 ]
Fei, Weiyang [1 ]
机构
[1] Tsinghua Univ, Dept Chem Engn, State Key Lab Chem Engn, Beijing 100084, Peoples R China
[2] Univ Melbourne, Dept Chem Engn, Parkville, Vic 3010, Australia
基金
中国国家自然科学基金;
关键词
Solvent extraction; Mass transfer; Single drop; Drop breakage and coalescence; CFD simulation; Population balance model; MASS-TRANSFER ENHANCEMENT; SURFACE-ACTIVE AGENTS; SECTIONAL QUADRATURE METHOD; FLUID DYNAMIC-BEHAVIOR; NUMERICAL-SIMULATION; MARANGONI CONVECTION; TRANSFER COEFFICIENT; SOLVENT-EXTRACTION; TERMINAL VELOCITY; IONIC LIQUID;
D O I
10.1016/j.cjche.2019.03.025
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The experimental and numerical investigations of single drop in liquid/liquid extraction system have been reviewed with particular focus on experimental techniques and computational fluid dynamic simulation approaches. Comprehensive surveys of available experimental techniques and numerical approaches for single drop rising and falling were given. Subsequently, single drop mass transfer was also reviewed both experimentally and numerically. Additionally, single drop breakage and coalescence process and the influencing factors were summarized and compared, so as to establish sub-models for population balance model. Future directions on single drop mass transfer, drop breakage and coalescence were suggested. It is believed that the single drop is a powerful tool to assist extraction process design from lab-scale to pilot-scale. (C) 2019 The Chemical Industry and Engineering Society of China, and Chemical Industry Press Co., Ltd. All rights reserved.
引用
收藏
页码:2857 / 2875
页数:19
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