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化学工业与工程 2013, Vol. 30 Issue (2) :45-52    DOI:
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加压鼓泡塔反应器中气液两相流CFD数值模拟
秦玉建,靳海波
1.北京化工大学化工学院; 2.北京石油化工学院
CFD Simulation of Gas-Liquid Flow in a Pressurized Bubble Column
 QIN  Yu-Jian, JIN  Hai-Bo
1.College of Chemical Engineering, Beijing University of Chemical Technology;2.Department of Chemical Engineering, Beijing Institute of Petrochemical Technology

摘要
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摘要 对加压气液鼓泡塔反应器内的气液两相流进行了二维数值模拟,模拟的压力为0.5~2.0 MPa,表观气速为0.120~0.312 m/s;模拟采用了Euler-Euler模型,并耦合了气泡群平衡模型(PBM)预测气泡尺寸,该模型考虑了气泡聚并与破碎对气泡的影响。液相湍流采用标准k-ε模型,两相间的作用力只考虑曳力。模拟获得了局部气含率、局部气/液相时均轴向速度及其径向分布等数据,并与实验结果进行比较。结果表明,局部气含率、局部气相速度模拟结果与实验结果吻合较好,局部液相速度径向分布特征模拟结果与文献结果相符。
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秦玉建
靳海波
关键词加压鼓泡塔   气液两相流   气泡群平衡模型   聚并   破碎     
Abstract: Numerical simulation of gas-liquid flow in a pressurized cylindrical bubble column with two-fluid approach were conducted for system pressures varying from 0.5 MPa to 2.0 MPa and superficial gas velocities from 0.120 m/s to 0.312 m/s. In the simulations, air is used as the gas phase and tap water as liquid phase. Euler-Euler model and population balance model (PBM) which predicted bubble size changes characterized were incorporated into the simulations. In the models, the effect of bubble breakup and coalescence were taken into consideration. A standard k-ε  turbulence model was used to describe liquid phase turbulence viscosity in the simulations. The simulations only adopted the drag force for inter phase momentum exchange. The time-averaged gas/liquid velocities and local gas holdups were obtained from the simulations. The time-averaged gas velocities and local gas hold-ups were compared with experimental data and showed good agreement between measured and predicted data. The radial profiles of liquid velocities were in good agreement with the results of the literatures.
Keywordspressurized bubble column reactor   gas-liquid flow   population balance model   coalescence   break-up     
Received 2012-05-22;
Fund:

国家自然科学基金资助项目(20776018)。

Corresponding Authors: 靳海波,电话:(010)81292074转18,E-mail: jinhaibo@bipt.edu.cn。     Email: jinhaibo@bipt.edu.cn
About author: 秦玉建(1986-),男,硕士研究生,从事两相流反应工程方面的研究。
引用本文:   
秦玉建, 靳海波.加压鼓泡塔反应器中气液两相流CFD数值模拟[J].  化学工业与工程, 2013,30(2): 45-52
QIN Yu-Jian, JIN Hai-Bo.CFD Simulation of Gas-Liquid Flow in a Pressurized Bubble Column[J].  Chemcial Industry and Engineering, 2013,30(2): 45-52
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