CFD modeling of hydrodynamic characteristics of a gas-liquid two-phase stirred tank

被引:55
|
作者
Wang, Hongna [1 ]
Jia, Xiaoqiang [2 ,3 ]
Wang, Xue [2 ,3 ]
Zhou, Zhengxi [2 ,3 ]
Wen, Jianping [2 ,3 ]
Zhang, Jinli [1 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Dept Chem Engn, Tianjin 300072, Peoples R China
[2] Tianjin Univ, Sch Chem Engn & Technol, Dept Biol Engn, Tianjin 300072, Peoples R China
[3] Tianjin Univ, Sch Chem Engn & Technol, Minist Educ, Key Lab Syst Bioengn, Tianjin 300072, Peoples R China
基金
国家高技术研究发展计划(863计划); 中国国家自然科学基金;
关键词
CFD; Modeling; Gas-liquid; Hydrodynamics; Stirred tank; BUBBLE-SIZE DISTRIBUTIONS; MASS-TRANSFER; LOCAL GAS; TRAILING VORTICES; LDA MEASUREMENTS; PIV MEASUREMENTS; RUSHTON TURBINE; FLOW; VESSEL; SIMULATION;
D O I
10.1016/j.apm.2013.05.032
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
A three-dimensional CFD model was developed in this work to simulate hydrodynamic characteristics of a gas-liquid two-phase stirred tank with two six-bladed turbines and four baffles, coupling of the Multiple Size Group model to determine bubble size distribution. Important hydrodynamic parameters of the multi-phase system such as volume-averaged overall and time-averaged local gas holdups and axial liquid velocities along time and transversal courses were simulated and analyzed in detail, under varied operating conditions (inlet air flow rate and impeller rotation speed). Model predictions of local transient gas holdup and liquid velocity distributions on vertical and horizontal sections of the tank were also carried out. The overall flow patterns were discussed in detail to assess the mixing. Bubble size distributions were further predicted to reveal the unique properties of gas phase. Experimental measurements of overall gas holdups and local axial liquid velocities were used to validate the developed model. (C) 2013 Elsevier Inc. All rights reserved.
引用
收藏
页码:63 / 92
页数:30
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