Shear-induced sedimentation in yield stress fluids

Stability of coarse particles against gravity is an important issue in dense suspensions (fresh concrete, foodstuff, etc.). On the one hand, it is known that they are stable at rest when the interstitial paste has a high enough yield stress; on the other hand, it is not yet possible to predict if a given material will remain homogeneous during a flow. Using MRI techniques, we study the time evolution of the particle volume fraction during the flows in a Couette geometry of model density-mismatched suspensions of noncolloidal particles in yield stress fluids. We observe that shear induces sedimentation of the particles in all systems, which are stable at rest. The sedimentation velocity is observed to increase with increasing shear rate and particle diameter, and to decrease with increasing yield stress of the interstitial fluid. At low shear rate (’plastic regime’), we show that this phenomenon can be modelled by considering that the interstitial fluid behaves like a viscous fluid–of viscosity equal to the apparent viscosity of the sheared fluid–in the direction orthogonal to shear. The behavior at higher shear rates, when viscous effects start to be important, is also discussed. We finally study the dependence of the sedimentation velocity on the particle volume fraction, and show that its modelling requires estimating the local shear rate in the interstitial fluid.

► We study the impact of a flow on settling of particles in yield stress fluids.
► Shear induces sedimentation of particles in all systems, which are stable at rest.
► Settling velocity increases with the particle diameter and the inverse Bingham number.
► This phenomenon is modeled in the limits of low and high Bingham numbers.
► Solid fraction increase both hinders settling and lowers viscous drag.