Intensification of gas-liquid two-phase flow and mass transfer in microchannels by sudden expansions

被引:32
作者
Zhang, Shizhe [1 ]
Zhu, Chunying [1 ]
Feng, Huisheng [1 ]
Fu, Taotao [1 ]
Ma, Youguang [1 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, State Key Lab Chem Engn, Tianjin 300072, Peoples R China
基金
中国国家自然科学基金;
关键词
Microchannel; Sudden expansion unit; Gas-liquid mass transfer; Energy consumption; CO2; ABSORPTION; AQUEOUS-SOLUTION; PRESSURE-DROP; TAYLOR FLOW; SLUG FLOW; HYDROGENATION; ENHANCEMENT; PERFORMANCE; SIMULATION; FLUID;
D O I
10.1016/j.ces.2020.116040
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The intensification of mass transfer of CO2 absorption into [Bmim][BF4] aqueous solution by continuous sudden expansion units was investigated experimentally in microchannels. The influences of two-phase flow rates and the number of sudden expansion units on pressure drop and volumetric mass transfer coefficient were studied systematically. The results indicate that the sudden expansion structure could remarkably enhance gas-liquid mass transfer. The enhancement factor of mass transfer increases with increasing the number of sudden expansion units and gas-liquid flow rate ratio, while the pressure drop has only slight elevation. The effective mass transfer enhancement efficiency was assessed according to the energy consumption and enhancement factor, which could achieve from 1.2 to 2.4, showing excellent mass transfer intensification effect of the sudden expansion structure. Moreover, a new correlation was proposed for predicting liquid side volumetric mass transfer coefficient. (c) 2020 Elsevier Ltd. All rights reserved.
引用
收藏
页数:9
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