Gas-liquid two-phase flow distribution in parallel micro-channels with different header and channels' orientations

被引:45
作者
Liu, Yanchu [1 ]
Sun, Wanchun [1 ]
Wu, Wei [1 ]
Wang, Shuangfeng [1 ]
机构
[1] South China Univ Technol, Sch Chem & Chem Engn, Key Lab Heat Transfer Enhancement & Energy Conser, Minist Educ, Guangzhou 510640, Guangdong, Peoples R China
基金
中国国家自然科学基金;
关键词
Two-phase flow; Phase distribution; Parallel micro-channels; Header; Orientation; Visualization; COMPACT HEAT-EXCHANGER; T-JUNCTION; ADIABATIC CONDITION; ANNULAR-FLOW; MICROCHANNELS; PATTERN; MALDISTRIBUTION; TUBES;
D O I
10.1016/j.ijheatmasstransfer.2017.05.029
中图分类号
O414.1 [热力学];
学科分类号
摘要
An experimental investigation was conducted to study the effect of header and channels orientations on the two-phase flow distribution in parallel micro-channels. The parallel micro-channels was composed of a header with hydraulic diameter of 0.667 mm and three parallel channels with hydraulic diameter of 0.500 mm, all with rectangle cross sections. Nitrogen and 0.03 wt% sodium dodecyl sulfate (SDS) solution were used as the test working fluids. The inlet superficial velocities of gas and liquid varied from 0.200 to 16.0 m/s and from 0.0246 to 0.650 m/s, respectively. The fluid dynamics of two-phase flow splitting in parallel micro-channels was captured by high speed recording technique and three flow patterns were observed at the inlet. It was found that the phase distribution characteristics of two-phase flow in parallel channels highly depended on the inlet flow patterns and the orientations of header and channels. For slug flow, a uniform phase distribution was achieved in horizontal header with vertically downward channels, whereas the distribution of slug-annular flow was improved in vertically upward header and horizontal channels. For annular flow, two-phase inhomogeneous distribution reached the highest when the header was vertically downward. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:767 / 778
页数:12
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