Experimental study on gas-liquid-liquid macro-mixing in a stirred tank
Experimental study on gas-liquid-liquid macro-mixing in a stirred tank
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搅拌槽内气-液-液宏观混合实验研究
DOI:
10.1016/j.ces.2012.03.035
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发表时间:
2012-06-18
影响因子:
4.7
通讯作者:
Mao, Zai-Sha
中科院分区:
文献类型:
--
作者:
Cheng, Dang;Cheng, Jingcai;Mao, Zai-Sha
In this paper, experimental data on the mixing time of the continuous phase and power consumption of gas-liquid-liquid dispersions in a mechanically agitated baffled tank are presented. The electrical conductivity method is taken for the measurement of mixing time and the shaft-torque method for power consumption measurement. Tap water is used as the continuous phase, and kerosene and air as the dispersed ones. The effects of probe/tracer injection position, agitation speed, type of impeller, clearance of impeller off tank bottom, oil volume fraction, gas holdup and physical properties of the dispersed liquids on the macro-mixing of the gas-liquid-liquid system have been investigated. The phenomenon of gas-liquid-liquid macro-mixing in a stirred tank is largely similar to that of liquid-liquid and gas-liquid stirred tanks. Our experiments indicate that the gas-liquid-liquid macro-mixing can be enhanced at higher gas holdups while damped at low gas holdups. Contrary to gas effect, the dispersed oil phase at low holdups increases the macro-mixing intensity but at higher holdups decreases the macro-mixing intensity of the continuous phase. The experimental results show that axial impellers are more energy efficient for gas-liquid-liquid macro-mixing than radial impellers. A simple correlation is developed for predicting the mixing time in gas-liquid-liquid three-phase systems and satisfactory agreement with experimental data is observed. (C) 2012 Elsevier Ltd. All rights reserved.