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    徐旭东, 张巍, 李伟锋, 刘海峰, 王辅臣. 十字型通道内黏弹性撞击流混合机理研究[J]. 华东理工大学学报(自然科学版), 2023, 49(3): 360-367. DOI: 10.14135/j.cnki.1006-3080.20220316001
    引用本文: 徐旭东, 张巍, 李伟锋, 刘海峰, 王辅臣. 十字型通道内黏弹性撞击流混合机理研究[J]. 华东理工大学学报(自然科学版), 2023, 49(3): 360-367. DOI: 10.14135/j.cnki.1006-3080.20220316001
    XU Xudong, ZHANG Wei, LI Weifeng, LIU Haifeng, WANG Fuchen. Mixing Mechanisms of Viscoelastic Impinging Flow in Cross-Shaped Channels[J]. Journal of East China University of Science and Technology, 2023, 49(3): 360-367. DOI: 10.14135/j.cnki.1006-3080.20220316001
    Citation: XU Xudong, ZHANG Wei, LI Weifeng, LIU Haifeng, WANG Fuchen. Mixing Mechanisms of Viscoelastic Impinging Flow in Cross-Shaped Channels[J]. Journal of East China University of Science and Technology, 2023, 49(3): 360-367. DOI: 10.14135/j.cnki.1006-3080.20220316001

    十字型通道内黏弹性撞击流混合机理研究

    Mixing Mechanisms of Viscoelastic Impinging Flow in Cross-Shaped Channels

    • 摘要: 采用激光诱导荧光(PLIF)技术对十字型通道中黏弹性流体(聚环氧乙烷溶液)进行可视化研究,重点考察了雷诺数(Re)、聚合物溶液质量分数(w)和通道尺度对流体流动模式、振荡特性以及混合效果的影响。结果表明,对于牛顿流体(水),随着雷诺数增加(20<Re<500),500 μm、6 mm和1 cm的十字型通道内均依次呈现分离流、稳态吞噬流、涡脱落振荡以及非稳态吞噬流;而对于黏弹性流体,随着聚合物溶液质量分数增加(0.01%≤w≤0.30%),流体弹性效应增强,在低聚合物溶液质量分数下微通道内出现了惯性弹性非稳态振荡,导致混合增强,而在较高质量分数下出现了弹性主导的非稳态振荡,弹性非稳态振荡在维森贝格数和雷诺数较低时具有周期性特征,随着维森贝格数和雷诺数增大,振荡周期减小且趋于不规则。对于6 mm和1 cm十字型通道,随着聚合物溶液质量分数的增加,涡脱落振荡和非稳态吞噬流的临界雷诺数增大,在较高聚合物溶液质量分数下非稳态吞噬流消失。

       

      Abstract: Recently, the microchannel has attracted wide attention due to its safety, reliability and high mixing performance. Most of the current researches focus on Newtonian fluids, but the liquids used in practical applications are often elastic and viscous. Therefore, the planar laser-induced fluorescence (PLIF) technique was used to visualize viscoelastic fluid (polyethylene oxide solution) in cross-shaped channels, focusing on the influence of Reynolds number, channel sizes and polymer solution mass fraction on flow regimes, oscillatory characteristics and mixing effect. For Newtonian fluid (pure water), the separation flow, steady engulfment flow, vortex shedding oscillations and unsteady engulfment flow were found with the increase of Reynolds number (20<Re<500) in all cross-shaped channels (500 μm, 6 mm and 1 cm). For viscoelastic fluid, as the polymer solution mass fraction increased (0.01%≤w≤0.30%), the fluid elastic effect was enhanced, where an inertioelastic unsteady oscillation occurred at low concentrations which enhanced mixing, and an elastic-dominated unsteady oscillation emerged at higher concentrations within the microchannel.The elastic-dominated unsteady oscillation had periodic characteristics at low Wi and Re. As Wi and Re increased, oscillation period decreased and the flow tended to be irregular. For the 6 mm and 1 cm cross-shaped channels, the critical Reynolds number of vortex shedding oscillations and the unsteady engulfment flow increased with the increase of concentrations, and the unsteady engulfment flow disappeared at higher concentrations.

       

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