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Investigation of instability in viscosity-stratified flow: Experiments and simulations.

机译:粘度分层流动中的不稳定性研究:实验和模拟。

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摘要

Static or motionless mixers are widely used in mixing operations. A typical inlet geometry to the static mixer is the centerline injector. An undesirable flow instability can occur under certain conditions downstream of the injector between the injected core-flow and the outer co-flow due to viscosity stratification at the interface. Experiments were performed to investigate a viscosity-stratified flow in a circular geometry using Laser Induced Fluorescence (LIF) and Particle Image Velocimetry (PIV). Two new flow patterns were observed for the first time. Moreover, the unstable interfacial waves displayed a spiral development along the centerline. The experimental results for stable and unstable regions are compared against analytical results. Time-averaged scalar dispersion and velocity profiles for the unstable region indicate a broadening of the core-flow as expected.; A front-tracking/finite difference method was used to investigate interfacial instabilities for a two-layer density-matched viscosity-stratified Poiseuille flow. The effect of Reynolds number, thickness ratio, viscosity ratio, and wavenumber on the growth rate of the instability was investigated. The simulation replicates experimental features such as the sharp curvature of the interface and the fingers penetrating from the more viscous fluid into the less-viscous layer. Results of linear and nonlinear instabilities are presented for different parameters. Next, we studied three-layer Poiseuille flow using the same method and concentrated on the large amplitude nonlinear instability. Results are presented for varying viscosity ratio, Weber number, and phase difference. Interfacial tension has a very strong effect on the evolution of the interface. The sinuous instability appears to evolve faster than the varicose one. The intruding high-viscosity finger exhibits a bulbous tip for certain parameters. Drop formation is precluded by the two-dimensional nature of the calculations.
机译:静态或静止混合器广泛用于混合操作。静态混合器的典型入口几何形状是中心线喷射器。由于界面处的粘性分层,在注入器下游的某些条件下,在注入的岩心流和外部同流之间可能会发生不期望的流动不稳定性。进行实验以研究使用激光诱导荧光(LIF)和粒子图像测速(PIV)的圆形几何形状的粘度分层流。首次观察到两个新的流动模式。此外,不稳定的界面波沿中心线呈螺旋状发展。将稳定和不稳定区域的实验结果与分析结果进行比较。不稳定区域的时间平均标量色散和速度曲线表明,岩心流如预期的那样变宽。使用前跟踪/有限差分方法来研究两层密度匹配的粘度分层的Poiseuille流的界面不稳定性。研究了雷诺数,厚度比,粘度比和波数对不稳定性生长速率的影响。该模拟复制了实验性功能,例如界面的急剧弯曲以及手指从粘度较高的流体渗透到粘度较低的层中。给出了针对不同参数的线性和非线性不稳定性的结果。接下来,我们使用相同的方法研究了三层Poiseuille流,并集中于大振幅非线性不稳定性。给出了变化的粘度比,韦伯数和相差的结果。界面张力对界面的演变有很大的影响。弯曲的不稳定性似乎比曲张的不稳定性快。对于某些参数,侵入的高粘度手指显示出球根形的尖端。计算的二维性质排除了液滴的形成。

著录项

  • 作者

    Cao, Qing.;

  • 作者单位

    University of Delaware.;

  • 授予单位 University of Delaware.;
  • 学科 Engineering Mechanical.
  • 学位 Ph.D.
  • 年度 2005
  • 页码 117 p.
  • 总页数 117
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 机械、仪表工业;
  • 关键词

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