CFD modeling of reactive absorption of CO2 in aqueous NaOH in a rectangular bubble column: Comparison of mass transfer and enhancement factor model

被引:23
|
作者
Liu, Junda [1 ]
Zhou, Ping [1 ]
Liu, Liu [1 ]
Chen, Si [1 ]
Song, Yanpo [1 ]
Yan, Hongjie [1 ]
机构
[1] Cent South Univ, Sch Energy Sci & Engn, Lushannan Rd 932, Changsha 410083, Peoples R China
基金
中国国家自然科学基金;
关键词
Bubble column; Two-phase flow; Chemical reaction; Mass transfer rate model; CFD; PLUME OSCILLATIONS; CHEMICAL-REACTION; CHEMISORPTION; HYDRODYNAMICS; FLOW;
D O I
10.1016/j.ces.2020.116218
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Presently various mass transfer rate models have been developed to predict the mass transfer rate in the column. Also, different enhancement factor models were proposed to include the influence of chemical reaction on mass transfer process. However, a comprehensive assessment of these models has rarely been performed, leaving the model accuracy arguable. In this study, four typical mass transfer rate models and two enhancement factor models were employed to simulate the gas-fluid mass transfer behaviors of a bubble plume rising in a rectangular bubble column, and their accuracies were evaluated by comparing the simulation results with the published experimental data. The results show that the Henket1 model is the most accurate among the assessed four mass transfer models. The model of Hlawitschka performs better than that with a constant enhancement factor. The mass transfer model has very little effect on pH variation at the end of the reaction. (C) 2020 Elsevier Ltd. All rights reserved.
引用
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页数:8
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