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化学工业与工程 2017, Vol. 34 Issue (6) :81-87    DOI: 10.13353/j.issn.1004.9533.20161066
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微通道中气-液-液三相流流型及传质研究
荀涛, 蔡旺锋, 张旭斌
天津大学化工学院, 天津 300350
The Flow Pattern and Mass Transfer of Gas-Liquid-LiquidThree Phase Flow in Microchannel
Xun Tao, Cai Wangfeng, Zhang Xubin
School of Chemical Engineering and Technology, Tianjin University, Tianjin 300350, China

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摘要 

使用双T型微通道,以体积分数为30%的磷酸三丁酯(TBP)的环己烷溶液-乙酸水溶液为萃取体系,研究了不同油水两相流量比及油水两相总流量条件下,气相的引入及气相流量分率α对流型及传质的影响,并获得总体积传质系数kLa与油水两相流量比q、气相雷诺数Reg、液相平均雷诺数ReM的关系式。研究结果表明,第1个T型接口处气相的引入所带来的气相剪切作用能促进第2个T型接口处分散相液滴的形成,可使液-液并行流转化为气-液-液三相弹状流;同时,由于气-液-液弹状流具有较高的相接触面积及内循环作用,传质系数kLa得到显著提高。

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荀涛
蔡旺锋
张旭斌
关键词微通道;   气-液-液弹状流;   流型;   传质系数     
Abstract

The double T-junction microchannel was used to research the flow pattern and mass transfer of gas-liquid-liquid three phase flow in microchannel.30% TBP(in cyclohexane)-acetic acid-water was chosen as extraction system,and air as inserting gas.Effect of void fraction expressed as α (ratio of gas volume flow rate to total volume flow rate) and volume ratio of organic phase to aqueous phase expressed as q on flow regime and mass transfer were experimentally investigated.The overall volumetric mean mass transfer coefficient kLa was correlated with q,Reynolds number of gas phase Reg and mean Reynolds number of liquid phase ReM.With the introduction of gas,gas-liquid-liquid slug flow can be formed instead of liquid-liquid parallel flow.The mass transfer coefficient of gas-liquid-liquid slug flow is also significantly enhanced because of the high dispersion of two immiscible liquid phase and the internal circulation effect.

Keywordsmicrochannel;   gas-liquid-liquid slug flow;   flow pattern;   mass transfer coefficient     
Received 2016-04-12;
Corresponding Authors: 张旭斌,E-mail:tjzxb@tju.edu.cn。     Email: tjzxb@tju.edu.cn
About author: 荀涛(1991-),男,硕士研究生,现从事微通道内流型及传质方面的研究。
引用本文:   
荀涛, 蔡旺锋, 张旭斌.微通道中气-液-液三相流流型及传质研究[J].  化学工业与工程, 2017,34(6): 81-87
Xun Tao, Cai Wangfeng, Zhang Xubin.The Flow Pattern and Mass Transfer of Gas-Liquid-LiquidThree Phase Flow in Microchannel[J].  Chemcial Industry and Engineering, 2017,34(6): 81-87
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