Carbon dioxide (CO2) absorption and interfacial mass transfer across vertically confined free liquid film-a numerical investigation

被引:23
作者
Hu, Jianguang [1 ]
Yang, Xiaogang [2 ]
Yu, Jianguo [1 ]
Dai, Gance [1 ]
机构
[1] East China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
[2] Univ Nottingham Ningbo China, Int Doctoral Innovat Ctr, Ningbo 315100, Zhejiang, Peoples R China
基金
浙江省自然科学基金;
关键词
Confined free liquid film; Mass transfer; Vorticity; Computational fluid dynamics (CFD); GAS-LIQUID; FLOW BEHAVIOR; FALLING FILM; SIMULATION; PACKINGS; WATER; DYNAMICS; EXCHANGE; VOLUME; PLATE;
D O I
10.1016/j.cep.2016.11.002
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
CO2 absorption by a confined free film has been investigated using the CFD approach. Particular attention focuses on the relationship between mass transfer and flow behaviour of the confined free film. Simulation results show that the average K-L value grows 26.9% for the open window region and 17.4% for the lower-wall region, respectively, in comparison to the values in the upper-wall region, and the average IQ value of confined free film along the flow direction is about 19.2% higher than the value of wall-bounded film, which affirms that the use of an open window can significantly enhance mass transfer performance and such effect also has impact on the entire regions. It was revealed that there exist two types of vortices inside the film, inner vortices and interfacial vortices. In addition, a correlation coefficient R-Omega c is proposed to provide a quantitative measure to characterise the relationship between the local mass concentration profile and vorticity distribution of confined free film. Simulation shows that the average value of R-Omega c is 0.93, indicating that the two parameters are highly correlated. Furthermore, the cause of lower correlation coefficient value is discussed. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:46 / 56
页数:11
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