Population Balance Modeling of Breakage and Coalescence of Dispersed Bubbles or Droplets in Multiphase Systems

被引:5
|
作者
Qin Chengpeng [1 ,2 ]
Yang Ning [1 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, State Key Laborary Multiphase Complex Syst, Beijing 100190, Peoples R China
[2] Univ Chinese Acad Sci, Beijing 100049, Peoples R China
基金
中国国家自然科学基金;
关键词
population balance model; coalescence; breakage; bubble; droplet; multiphase flow; INTERFACIAL AREA TRANSPORT; LIQUID-LIQUID DISPERSIONS; DIRECT QUADRATURE METHOD; DEVELOPED TURBULENT-FLOW; NONIDEAL STIRRED-TANK; SIZE DISTRIBUTIONS; CFD SIMULATION; HIGH-PRESSURE; 2-PHASE FLOW; NUMERICAL-SIMULATION;
D O I
10.7536/PC160416
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Modeling of breakage and coalescence of dispersed phases such as bubbles or droplets in multiphase systems is of paramount importance to the control of the dispersed phase size distribution in process industry. Population balance model (PBM) has become a rountine tool to simulate the breakage, coalescence and size distribuiton of dispersed phase. However, the current kernel functions for breakage and coalescence in PBM are either derived from statistical models or based on some phenomenological models, empirical correlations or semi theoretical methods, since the physics of breakage and coalescence in multi-phase systems is complex. As a result, few models could completely considers all of the physical constraints relevant to the complex flow field and material properties, and it is still a challenging issue to accurately predict the breakage and coalescence for different operating conditions. This article gives a systematic overview of the mechanisms and models about the breakage and coalescence of bubbles or droplets, and the numerical algothirm for population balance equations as well as the application of PBM simulation in gas-liquid or liquid-liquid systems. Finally, the state-of-the-art and future development of PBM are analyzed.
引用
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页码:1207 / 1223
页数:17
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