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缩放管中黏弹性流体电渗压力混合流模拟研究

杜昌隆 夏威豪 杨嘉杰 李捷

杜昌隆, 夏威豪, 杨嘉杰, 李捷. 缩放管中黏弹性流体电渗压力混合流模拟研究[J]. 应用数学和力学, 2023, 44(6): 643-653. doi: 10.21656/1000-0887.430255
引用本文: 杜昌隆, 夏威豪, 杨嘉杰, 李捷. 缩放管中黏弹性流体电渗压力混合流模拟研究[J]. 应用数学和力学, 2023, 44(6): 643-653. doi: 10.21656/1000-0887.430255
DU Changlong, XIA Weihao, YANG Jiajie, LI Jie. Simulation of Electroosmotic and Pressure-Driven Mixed Flow of Viscoelastic Fluids in Converging-Diverging Tubes[J]. Applied Mathematics and Mechanics, 2023, 44(6): 643-653. doi: 10.21656/1000-0887.430255
Citation: DU Changlong, XIA Weihao, YANG Jiajie, LI Jie. Simulation of Electroosmotic and Pressure-Driven Mixed Flow of Viscoelastic Fluids in Converging-Diverging Tubes[J]. Applied Mathematics and Mechanics, 2023, 44(6): 643-653. doi: 10.21656/1000-0887.430255

缩放管中黏弹性流体电渗压力混合流模拟研究

doi: 10.21656/1000-0887.430255
详细信息
    作者简介:

    杜昌隆(1996—),男,硕士生(E-mail: ducl1025@qq.com)

    通讯作者:

    李捷(1982—),男,副教授,博士生导师(通讯作者. E-mail: jieli@whut.edu.cn)

  • 中图分类号: O357.3

Simulation of Electroosmotic and Pressure-Driven Mixed Flow of Viscoelastic Fluids in Converging-Diverging Tubes

  • 摘要: 电渗压力混合流已广泛应用于各种生化微流控领域中,其中黏弹性流体的弹性不稳定性不可忽视.采用黏弹性流体,对10∶1∶10的微通道缩放管中电渗压力混合驱动流动进行数值仿真.研究了不同压力和不同聚合物浓度对流体流动的影响,并分析了Newton流体与黏弹性流体在缩放管中速度分布的叠加原理.结果表明:反向压力使黏弹性流体展现出更大的不稳定性,使得入口涡流变大,压力每增大1 Pa涡流变大25 μm,而正向压力使涡流变小.较小反向压力时,入口涡流随着聚合物浓度的增大而增大,并逐渐趋于稳定.在较大反向压力下,涡流大小随着聚合物浓度的增大先升后降.
  • 图  1  几何结构示意图

    Figure  1.  The structure diagram of the microchannel

    图  2  Γ=2速度分布验证

    Figure  2.  For Γ=2, the velocity distribution verification

    图  3  p=0 Pa, Cp=300 ppm, E=20 V,不同时刻的流线

      为了解释图中的颜色,读者可以参考本文的电子网页版本,后同.

    Figure  3.  For p=0 Pa, Cp=300 ppm, E=20 V, the streamlines at different moments

    图  4  pout=3 Pa, Cp=300 ppm, E=20 V,不同时刻的流线

    Figure  4.  For pout=3 Pa, Cp=300 ppm, E=20 V, the streamlines at different moments

    图  5  3个不同位置的速度随时间的变化

    Figure  5.  The change of the velocity with time at 3 different locations

    图  6  x=0,沿y轴的速度分布

    Figure  6.  The velocity distributions along the y axis

    图  7  Cp=300 ppm,入口处电势E=20 V,t=0.8 s时刻下的流线,pout=0 Pa,采用不同的进口压力

    Figure  7.  For Cp=300 ppm, entrance potential E=20 V, the streamlines at t=0.8 s, pout=0 Pa, with different inlet pressures

    图  8  涡流大小示意图

    Figure  8.  Schematic diagram of the vortex size

    图  9  E=20 V, Cp=300 ppm: 涡流大小随时间大小波动和不同出口压力下涡流的平均大小

    Figure  9.  For E=20 V, Cp=300 ppm: the vortex current size changing with time and the vortex current sizes under different outlet pressures

    图  10  E=20 V,涡流大小随聚合物浓度的变化

    Figure  10.  For E=20 V, the change of the vortex size with the polymer concentration

    图  11  通道中点速度的离散系数

    Figure  11.  The dispersion coefficient of the midpoint velocity of the channel

    图  12  pout=5 Pa,沿y轴的速度分布

    Figure  12.  The velocity distributions along the y- axis, pout=5 Pa

    表  1  模型部分参数

    Table  1.   Numerical simulation parameters

    parameter name value
    ρ/(kg/m3) 1 000
    ηs/(Pa·s) 0.001
    E0/(V/m) 20 000
    ζ/mV -110
    C0/(mol/m3) 0.01
    T/K 300
    下载: 导出CSV
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出版历程
  • 收稿日期:  2022-08-08
  • 修回日期:  2023-02-15
  • 刊出日期:  2023-06-01

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