{"title":"Water-Oil Flow in Square Microchannels With a Crossed Junction","authors":"Z. Cao, Zan Wu, J. Qian, B. Sundén","doi":"10.1115/FEDSM2018-83056","DOIUrl":null,"url":null,"abstract":"In the present study, water-oil flow patterns and slug hydrodynamics were experimentally studied in square glass microchannels with various hydraulic diameters (Dh = 600 μm, 400 μm, 200 μm). The aqueous phase is the continuous phase while the organic phase is the dispersed phase. The ranges of flow rates of the continuous phase and the dispersed phase are 0–200 ml/h and 0–12 ml/h, 0–120 ml/h and 0–6 ml/h, and 0–60 ml/h and 0–2 ml/h in the microchannels with Dh = 600 μm, 400 μm and 200 μm, respectively. The results show that the hydraulic diameter has significant effects on flow patterns and three main flow patterns are observed, i.e., annular flow, slug flow and droplet flow. Generally, annular flow appeared at high flow rates of the dispersed phase and low flow rates of the continuous phase, while droplet flow appeared at low flow rates of the dispersed phase and high flow rates of the continuous phase. However, slug flow existed at comparable flow rates of the continuous and dispersed phases. A dimensionless analysis is carried out and a new dimensionless group including Weber number and Reynolds number is derived. The new defined dimensionless group performs well to develop a general flow pattern map. In addition, slug flow hydrodynamics are investigated as well in the present study, considering the slug length and slug velocity. Based on the present experimental results, a new scaling law is proposed to predict the slug length and it shows a good agreement with the experimental results. It has been widely reported that slug velocities depend linearly on the total flow rates of the two phases, which is consistent with the present study. The linear law provides a good prediction of the experimental slug velocities but different slopes are suggested in microchannels with different hydraulic diameters.","PeriodicalId":285631,"journal":{"name":"Volume 3: Fluid Machinery; Erosion, Slurry, Sedimentation; Experimental, Multiscale, and Numerical Methods for Multiphase Flows; Gas-Liquid, Gas-Solid, and Liquid-Solid Flows; Performance of Multiphase Flow Systems; Micro/Nano-Fluidics","volume":"29 1","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"2018-07-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Volume 3: Fluid Machinery; Erosion, Slurry, Sedimentation; Experimental, Multiscale, and Numerical Methods for Multiphase Flows; Gas-Liquid, Gas-Solid, and Liquid-Solid Flows; Performance of Multiphase Flow Systems; Micro/Nano-Fluidics","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1115/FEDSM2018-83056","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
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Abstract

In the present study, water-oil flow patterns and slug hydrodynamics were experimentally studied in square glass microchannels with various hydraulic diameters (Dh = 600 μm, 400 μm, 200 μm). The aqueous phase is the continuous phase while the organic phase is the dispersed phase. The ranges of flow rates of the continuous phase and the dispersed phase are 0–200 ml/h and 0–12 ml/h, 0–120 ml/h and 0–6 ml/h, and 0–60 ml/h and 0–2 ml/h in the microchannels with Dh = 600 μm, 400 μm and 200 μm, respectively. The results show that the hydraulic diameter has significant effects on flow patterns and three main flow patterns are observed, i.e., annular flow, slug flow and droplet flow. Generally, annular flow appeared at high flow rates of the dispersed phase and low flow rates of the continuous phase, while droplet flow appeared at low flow rates of the dispersed phase and high flow rates of the continuous phase. However, slug flow existed at comparable flow rates of the continuous and dispersed phases. A dimensionless analysis is carried out and a new dimensionless group including Weber number and Reynolds number is derived. The new defined dimensionless group performs well to develop a general flow pattern map. In addition, slug flow hydrodynamics are investigated as well in the present study, considering the slug length and slug velocity. Based on the present experimental results, a new scaling law is proposed to predict the slug length and it shows a good agreement with the experimental results. It has been widely reported that slug velocities depend linearly on the total flow rates of the two phases, which is consistent with the present study. The linear law provides a good prediction of the experimental slug velocities but different slopes are suggested in microchannels with different hydraulic diameters.
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具有交叉结的方形微通道中的水-油流动
在不同水力直径(Dh = 600 μm, 400 μm, 200 μm)的方形玻璃微通道中,实验研究了水-油流动模式和段塞流体动力学。水相为连续相,有机相为分散相。在Dh = 600 μm、400 μm和200 μm的微通道中,连续相和分散相的流速范围分别为0 ~ 200 ml/h和0 ~ 12 ml/h, 0 ~ 120 ml/h和0 ~ 6 ml/h, 0 ~ 60 ml/h和0 ~ 2 ml/h。结果表明:水力直径对流动形态有显著影响,主要有三种流动形态:环空流动、段塞流动和液滴流动。一般来说,环空流动出现在分散相的高流速和连续相的低流速时,而液滴流动出现在分散相的低流速和连续相的高流速时。然而,在连续相和分散相流速相当的情况下,段塞流仍然存在。进行了无因次分析,导出了包括韦伯数和雷诺数在内的新的无因次群。新定义的无量纲群在开发通用流型图方面表现良好。此外,考虑段塞流长度和段塞流速度,本文还对段塞流流体动力学进行了研究。在现有实验结果的基础上,提出了一种新的预测段塞长度的标度律,与实验结果吻合较好。已有广泛报道,段塞流速度与两相的总流速呈线性关系,这与本研究结果一致。线性规律可以很好地预测实验段塞流速度,但在不同水力直径的微通道中,建议采用不同的斜率。
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