A generalized equation for rheology of emulsions and suspensions of deformable particles subjected to simple shear at low Reynolds number
Author(s) -
Salah A. Faroughi,
Christian Huber
Publication year - 2014
Publication title -
rheologica acta
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.775
H-Index - 80
eISSN - 1435-1528
pISSN - 0035-4511
DOI - 10.1007/s00397-014-0825-8
Subject(s) - rheology , reynolds number , capillary number , mechanics , weissenberg number , shear rate , viscosity , thermodynamics , volume fraction , materials science , capillary action , shear flow , simple shear , physics , shear stress , flow (mathematics) , turbulence
We present analyses to provide a generalized rheological equation for suspensions and emulsions of non-Brownian particles. These multiparticle systems are subjected to a steady straining flow at low Reynolds number. We first consider the effect of a single deformable fluid particle on the ambient velocity and stress fields to constrain the rheological behavior of dilute mixtures. In the homogenization process, we introduce a first volume correction by considering a finite domain for the incompressible matrix. We then extend the solution for the rheology of concentrated system using an incremental differential method operating in a fixed and finite volume, where we account for the effective volume of particles through a crowding factor. This approach provides a self-consistent method to approximate hydrodynamic interactions between bubbles, droplets, or solid particles in concentrated systems. The resultant non-linear model predicts the relative viscosity over particle volume fractions ranging from dilute to the the random close packing in the limit of small deformation (capillary or Weissenberg numbers) for any viscosity ratio between the dispersed and continuous phases. The predictions from our model are tested against published datasets and other constitutive equations over different ranges of viscosity ratio, volume fraction, and shear rate. These comparisons show that our model, is in excellent agreement with published datasets. Moreover, comparisons with experimental data show that the model performs very well when extrapolated to high capillary numbers (C a≫1). We also predict the existence of two dimensionless numbers; a critical viscosity ratio and critical capillary numbers that characterize transitions in the macroscopic rheological behavior of emulsions. Finally, we present a regime diagram in terms of the viscosity ratio and capillary number that constrains conditions where emulsions behave like Newtonian or Non-Newtonian fluids
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