CFD investigation of the gas dispersion and liquid mixing in bubble columns with dense vertical internals

被引:20
作者
Agahzamin, Siamak [1 ]
Pakzad, Leila [1 ]
机构
[1] Lakehead Univ, Dept Chem Engn, 955 Oliver Rd, Thunder Bay, ON P7B 5E1, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Bubble column; Dense internals; Gas dispersion; Liquid mixing; CFD; PHASE DISPERSION; AXIAL-DISPERSION; MASS-TRANSFER; FLUID-DYNAMICS; EULERIAN SIMULATIONS; NUMERICAL-SIMULATION; FLOW; HOLDUP; REACTORS; MODEL;
D O I
10.1016/j.ces.2019.03.048
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Bubble columns are widely equipped with vertical internals for heat removal in slurry/bubble column reactors or providing the light source in photobioreactors. Understanding the effect of internals on the hydrodynamics of a bubble column reactor is crucial for the reactor design and scale-up. The gas dispersion and liquid mixing are two important parameters in design of bubble columns. In this study, the Eulerian-Eulerian simulation coupled with the population balance model was developed for the bubble column with dense vertical internals. The impulse tracer injection was applied to study the gas dispersion. The effect of the gas flow fluctuations, the time span of tracer injection, and the presence of internals was assessed at different superficial gas velocities. The results showed that the presence of internals has a notable effect on gas behavior. A stronger gas velocity gradient with less turbulence and dispersion were observed in the presence of internals. To study the liquid mixing, the tracer technique was applied, and the sensitivity of results to the tracer injection and detector points have been discussed. The presence of internals reduced the fluctuating liquid velocities, which led to a lower mixing performance in the bubble column. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页码:425 / 438
页数:14
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