Enhancement effect and mechanism of gas-liquid mass transfer by baffles embedded in the microchannel

被引:38
|
作者
Yin, Yaran [1 ]
Zhu, Chunying [1 ]
Fu, Taotao [1 ]
Ma, Youguang [1 ]
Wang, Kai [2 ]
Luo, Guangsheng [2 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, State Key Lab Chem Engn, Tianjin 300072, Peoples R China
[2] Tsinghua Univ, Dept Chem Engn, State Key Lab Chem Engn, Beijing 100084, Peoples R China
关键词
Mass transfer enhancement; Microchannel; Gas-liquid two-phase; Baffle; Enhancement factor; CO2; ABSORPTION; CARBON-DIOXIDE; AQUEOUS-SOLUTIONS; HEAT-TRANSFER; TAYLOR FLOW; SLUG FLOW; CAPTURE; MONOETHANOLAMINE; PERFORMANCE; REACTORS;
D O I
10.1016/j.ces.2019.02.039
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The enhancement of gas-liquid mass transfer by baffles embedded in a microchannel was investigated experimentally for CO2 absorption into monoethanolamine/1-butyl-3-methylimidazolium tetrafluoroborate (MEA/Bmim][BF4]) aqueous solutions. The influences of baffle size on mass transfer rate and pressure drop were studied through varying the MEA/[Bmim][BE4] concentration ratio, gas-liquid flow rate and blockage ratio. Experimental results showed that the proper baffle configuration could improve effectively gas-liquid mass transfer performance. Although the pressure drop of the baffled microchannel has slight increase (the maximum growth 0.3 kPa, or 20% in relative term) in comparison with the unobstructed microchannel, it is acceptable for industrial application. Under lower MEA/[Bmim][BE4] concentration ratios, higher two-phase flow rates and blockage ratios, the mass transfer enhancement is more pronounced and the enhancement factor could reach to 1.5. A new empirical correlation of enhancement factor is proposed with good predictive performance. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页码:264 / 273
页数:10
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