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Particle migration rates in a Couette apparatus

机译:Couette设备中的粒子迁移率

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Bulk migration of particles towards regions of lower shear occurs in suspensions of neutrally buoyant spheres in Newtonian fluids undergoing creeping flow in the annular region between two rotating, coaxial cylinders (a wide-gap Couette). For a monomodal suspension of spheres in a viscous fluid, dimensional analysis indicates that the rate of migration at a given concentration should scale with the square of the sphere radius. However, a previous experimental study [12] showed that the rate of migration of spherical particles at 50% volume concentration actually scaled with the sphere radius to approximately the 2.9 power. In the current study, a series of experiments is performed to extend the previous study to two new concentrations, namely, 35% and 42.5%. The new study indicates that the power scaling decreases with concentration.
机译:颗粒向较低剪切区域的大量迁移发生在牛顿流体中的中性浮球的悬浮液中,该悬浮液在两个旋转的同轴圆柱体(宽间隙Couette)之间的环形区域中经历蠕变流。对于球体在粘性流体中的单峰悬浮体,尺寸分析表明,在给定浓度下的迁移速率应与球体半径的平方成比例。但是,先前的一项实验研究[12]表明,球形粒子在体积浓度为50%时的迁移速率实际上与球形半径成比例,约为2.9幂。在当前的研究中,进行了一系列实验以将以前的研究扩展到两个新浓度,即35%和42.5%。这项新的研究表明,功率定标随浓度降低。

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