The flow of a very concentrated slurry in a parallel-plate device: influence of gravity

TL;DR

This study combines experiments and modeling to analyze the flow and structure of a highly concentrated slurry between horizontal plates, highlighting gravity's influence on phase configuration and flow profiles.

Contribution

It introduces a mean field model for concentrated slurry flow that accounts for gravity and predicts phase configurations and flow profiles.

Findings

Model accurately describes experimental velocity and stress data.

Gravity significantly influences slurry phase distribution.

Nonlinear flow and concentration profiles are predicted by the model.

Abstract

We investigate, both experimentally and theoretically, the fow and structure of a slurry when sheared between 2 horizontal plates. The slurry, otherwise called a "wet granular material", is made of non-Brownian particles immersed in a viscous fluid. The particles are heavier than the fluid, consequently, gravity influences the structure and flow profiles of the sheared material. Experiments are carried out in a plane Couette device, with a model slurry composed of approximately monodisperse spherical PMMA particles in oil, at high average solid concentration (about 58%). Optical observation reveals a typical 2-phase configuration, with a fluidized layer in contact with the upper plate and on top of an amorphous solid phase. We provide data on velocity profiles, wall-slip and shear stress versus the average shear rate. To interpret the data, we propose a model for the ideal case of infinite horizontal flat plates. The model, of mean field type, is based on local constitutive equations for the tangential and normal components of the stress tensor and on expressions relating the material viscometric coefficients (the shear viscosity eta and the normal viscosity psi) with the local concentration (phi) and the local shear rate. 1-,2- and 3-phase configurations are predicted, with non linear flow and concentration profiles. We conclude that the model equations correctly describe the experimental data, provided that appropriate forms are chosen for the divergence of eta and psi near the packing concentration (phi_max), namely a (phi_max-phi)^-1 singularity.