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Particle migration rates in a Couette apparatus

机译:耦合装置中的颗粒迁移速率

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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:在牛顿流体中的牛排流动在两个旋转的同轴圆柱(宽间隙耦合)之间的环形区域中的牛顿流体中的中性浮力球的悬浮液中,粒子迁移颗粒的块状迁移。对于粘性流体中的球形的单阳极悬浮液,尺寸分析表明给定浓度的迁移速率应与球半径的平方缩放。然而,先前的实验研究[12]表明球形颗粒在50%体积浓度下迁移的速度实际上与球半径缩放到大约2.9功率。在目前的研究中,进行一系列实验以将先前的研究延伸到两项新浓度,即35%和42.5%。新研究表明电力缩放随着浓度降低。

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