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Shear thinning in non-Brownian suspensions explained by variable friction between particles

Published online by Cambridge University Press:  10 December 2018

Laurent Lobry ,
Elisabeth Lemaire ,
Frédéric Blanc ,
Stany Gallier  and
François Peters Open the ORCID record for François Peters [Opens in a new window]
Laurent Lobry
Affiliation:
Institut de Physique de Nice, CNRS UCA, Parc Valrose, 06108 Nice CEDEX 2, France
Elisabeth Lemaire
Affiliation:
Institut de Physique de Nice, CNRS UCA, Parc Valrose, 06108 Nice CEDEX 2, France
Frédéric Blanc
Affiliation:
Institut de Physique de Nice, CNRS UCA, Parc Valrose, 06108 Nice CEDEX 2, France
Stany Gallier
Affiliation:
ArianeGroup, Le Bouchet Research Center, 91710 Vert le Petit, France
François Peters*
Affiliation:
Institut de Physique de Nice, CNRS UCA, Parc Valrose, 06108 Nice CEDEX 2, France
*
†Email address for correspondence: francois.peters@unice.fr
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Abstract

We propose to explain shear-thinning behaviour observed in most concentrated non-Brownian suspensions by variable friction between particles. Considering the low magnitude of the forces experienced by the particles of suspensions under shear flow, it is first argued that rough particles come into solid contact through one or a few asperities. In such a few-asperity elastic–plastic contact, the friction coefficient is expected not to be constant but to decrease with increasing normal load. Simulations based on the force coupling method and including such a load-dependent friction coefficient are performed for various particle volume fractions. The results of the numerical simulations are compared to viscosity measurements carried out on suspensions of polystyrene particles ($40~\unicode[STIX]{x03BC}\text{m}$ in diameter) dispersed in a Newtonian silicon oil. The agreement is shown to be satisfactory. Furthermore, the comparison between the simulations conducted either with a constant or a load-dependent friction coefficient provides a model for the shear-thinning viscosity. In this model the effective friction coefficient $\unicode[STIX]{x1D707}^{eff}$ is specified by the effective normal contact force which is simply proportional to the bulk shear stress. As the shear stress increases, $\unicode[STIX]{x1D707}^{eff}$ decreases and the jamming volume fraction increases, leading to the reduction of the viscosity. Finally, using this model, we show that it is possible to evaluate the microscopic friction coefficient for each applied shear stress from the rheometric measurements.

JFM classification

Complex Fluids: Complex Fluids Non-Newtonian Flows: Rheology Complex Fluids: Suspensions
Type
JFM Papers
Information
Journal of Fluid Mechanics , Volume 860 , 10 February 2019 , pp. 682 - 710
Copyright
© 2018 Cambridge University Press 

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