4.3 Article

Wall Effects on Spheres Settling Through Non-Newtonian Fluid Media in Cylindrical Tubes

Journal

JOURNAL OF DISPERSION SCIENCE AND TECHNOLOGY
Volume 36, Issue 9, Pages 1199-1207

Publisher

TAYLOR & FRANCIS INC
DOI: 10.1080/01932691.2014.966309

Keywords

Carreau viscosity model; eccentric effect; settling velocity; viscoelastic; wall factor

Funding

  1. Program for Changjiang Scholars and Innovative Research Team in University [IRT1294]

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Experimental study is performed to understand and quantify the wall and eccentric retardation effects on spheres settling in shear thinning and shear-thinning viscoelastic fluids over a wide range of diameter ratios (0.02 < lambda < 0.9). The four-parameter Carreau viscosity equation has been chosen to represent the apparent viscosity-shear rate of polyacrylamide solutions. Two new wall factor corrections are presented with excellent agreement compared to experimental data. The terminal settling velocity of a sphere in bounded fluid is significantly reduced by the presence of confining boundaries, named wall retardation effect that decreases due to the shear-thinning behavior of power law fluids, which is weaken further by the elastic effect of viscoelastic fluids. The wall factors of spheres settling in viscoelastic fluids increase at low xi up to 50, followed by a horizontal confidence region (0.7 <= f <= 1) at high In this region, the wall factor is mainly dominated by fluids' elasticity, which is more distinguished for small spheres. As the settling spheres approach to the wall (blR -> 1), the neighboring wall exert more intensive retardation that reduce the terminal settling velocity greatly when blR > 0.6 in pure shear-thinning fluids, and the extra retardation effect of nearby wall increases at high concentration due to the enhanced non-Newtonian property. In contrast, the eccentric effect on settling velocity in viscoelastic fluids is cut down greatly by the fluid's elasticity, which is negligible.

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