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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.
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页码:264 / 273
页数:10
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