Numerical investigation of gas-liquid and liquid-liquid Taylor flow through a circular microchannel with a sudden expansion

被引:6
|
作者
Etminan, Amin [1 ]
Muzychka, Yuri S. [1 ]
Pope, Kevin [1 ]
机构
[1] Mem Univ Newfoundland MUN, Fac Engn & Appl Sci, Dept Mech Engn, St John, NF A1B 3X5, Canada
来源
基金
加拿大自然科学与工程研究理事会;
关键词
gas-liquid; liquid-liquid; microchannel; numerical simulation; sudden expansion; SHARP FLUID INTERFACES; 2-PHASE FLOW; PRESSURE-DROP; MASS-TRANSFER; PATTERN TRANSITIONS; MULTIPHASE FLOW; SEGMENTED FLOW; HEAT-TRANSFER; SLUG FLOW; MU-PIV;
D O I
10.1002/cjce.24229
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper investigates a CFD-based analysis for gas-liquid and liquid-liquid Taylor flows through a circular axisymmetric microchannel with a sudden enlargement. A series of simulations are conducted by exploring the influence of different superficial velocity ratios, apparent viscosities, and channel expansion on the hydrodynamics of slug flow. A concentric junction introduces dispersed airflow into a continuous flow of water for gas-liquid flow, and the junction introduces dispersed water into a continuous flow of dodecane for liquid-liquid flow. The air-bubble and water-slug evolution processes, slug breakup, and slug expansion are investigated. In all cases, the lengths of air bubbles and water slugs increase with increasing superficial velocity ratio, particularly before the expansion. For gas-liquid flow, the apparent viscosity ratio causes a fluctuating interface over the uniform film region. However, the water slug length is shorter and the film region is slightly thicker in liquid-liquid compared to gas-liquid flow. The numerical analysis developed in this paper is in good agreement with the existing correlations and experimental data in the literature.
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页码:1596 / 1612
页数:17
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