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首页> 外文期刊>Experimental Thermal and Fluid Science: International Journal of Experimental Heat Transfer, Thermodynamics, and Fluid Mechanics >Characteristics of gas-liquid two-phase flows through a sudden contraction in rectangular microchannels
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Characteristics of gas-liquid two-phase flows through a sudden contraction in rectangular microchannels

机译:矩形微通道中气液两相流突然收缩的特性

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A series of experiments were conducted to study the effects of contraction ratio and different liquid properties on gas liquid two-phase flow through sudden contraction in micro-channel. Two rectangular microchannels with different contraction ratio were used. The widths of the larger channels upstream of the contraction were 0.53 or 0.78 mm (0.230 mm in height), while those of the smaller ones were fixed at 0.270 mm (0.230 mm in height). Distilled water, ethanol 49 wt% aqueous solution, pure ethanol and hydrofluoroether (HFE)-7200 were used as the test liquids, and nitrogen as the test gas. Flow pattern, bubble length, liquid slug length and bubble velocity were determined by analyzing video images of the flows. In addition, pressure profile upstream and downstream from the contraction was also measured for single-phase and two-phase flows. The pressure loss due to the contraction was determined from the pressure profiles. In the analysis, bubble velocity data and the pressure loss data were compared with calculations by some correlations in literatures. The bubble velocity data both upstream and downstream from the contraction were correlated with Kawahara et al.'s correlation (2010) where the correlation was accounted for aspect ratio of the channel. The correlation of the contraction coefficient for single-phase liquid flows was newly developed with Reynolds number and contraction ratio. The two-phase pressure drop data reasonably agreed with a slip flow model combined with the present contraction coefficient correlation and drift flux model based void fraction correlation. Moreover, numerical simulations were performed using the computational fluid dynamics software FLUENT (Fluent Inc.) and the volume of fluid (VOF) model. The present numerical simulation data agreed well with the experimental data for flow pattern, bubble velocity, bubble length, bubble pitch and pressure changes through the contraction. (C) 2015 Elsevier Inc. All rights reserved.
机译:进行了一系列实验,研究了收缩率和不同的液体性质对微通道中突然收缩的气液两相流的影响。使用两个具有不同收缩率的矩形微通道。收缩上游的较大通道的宽度为0.53或0.78毫米(高0.230毫米),而较小通道的宽度固定为0.270毫米(高0.230毫米)。将蒸馏水,49重量%的乙醇水溶液,纯乙醇和氢氟醚(HFE)-7200用作测试液体,并将氮气用作测试气体。通过分析流动的视频图像确定流动方式,气泡长度,液塞长度和气泡速度。另外,还测量了单相和两相流收缩后上游和下游的压力分布。由压力曲线确定由于收缩引起的压力损失。在分析中,通过文献中的一些相关性将气泡速度数据和压力损失数据与计算结果进行了比较。收缩上游和下游的气泡速度数据与Kawahara等人的相关性(2010年)相关,其中相关性考虑了通道的纵横比。利用雷诺数和收缩率新开发了单相液体收缩系数的相关性。两相压降数据与滑流模型合理结合,并与当前的收缩系数相关性和基于孔隙率相关性的漂移通量模型相结合。此外,使用计算流体动力学软件FLUENT(Fluent Inc.)和流体体积(VOF)模型进行了数值模拟。目前的数值模拟数据与通过收缩的流动模式,气泡速度,气泡长度,气泡间距和压力变化的实验数据非常吻合。 (C)2015 Elsevier Inc.保留所有权利。

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