Numerical simulations of dense granular suspensions in laminar flow under constant and varying shear rates
Sudharsan Srinivasan, Harry E.A. Van den Akker, Orest Shardt
2021
Computers & Fluids
Using an immersed boundary-lattice Boltzmann method, we investigated the response of dense granular suspensions to time-varying shear rates and flow reversals. The evolution of the relative apparent viscosity and particle structures was analysed. The concentration of solids (φ v ) and particle Reynolds numbers (Re p ) were varied over the ranges 6% ≤ φ v ≤ 47% and 0.105 ≤ Re p ≤ 0.529. The simulations included sub-grid scale corrections for unresolved lubrication forces and torques (normal and
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... angential). When φ v surpasses 30%, the contribution of the tangential lubrication corrections to the shear stress is dominant. While for intermediate solids fractions we find weak shear-thinning, we see weak shear-thickening for φ v > 40%. We show how the structure and apparent viscosity of a suspension evolves after a reversal of the shear direction. For 47% solids, simulations with step changes in the shear rate show the effects of the previous shear history on the viscosity of the suspension. J o u r n a l P r e -p r o o f Journal Pre-proof sions is typical practice in many processes, such as wastewater treatment, drilling operations, and ore refining plants, operating such transport lines frequently results in significant disruptions. Improved understanding of the complicated dynamics of particle-particle and fluid-particle interactions is thus highly desirable. Specifically, changes in the rheology and structure that occur due to the effects of flow reversals and abrupt shifts in the shear rate are of particular interest to us, as the transport of slurry involves such phenomena in bends, fittings, and valves. In our previous study (Srinivasan et al., 2020), we explored the effects of steady shear rate on rheology by implementing a spring-like force to handle particle collisions. In this paper, we improve the modelling of interparticle interactions by applying explicit lubrication corrections over sub-grid scale distances, so that the resulting simulation can provide a better understanding of both the steady-state and transient rheological behaviour of granular suspensions. We restrict ourselves to suspensions of particles typically some 300 micron in diameter, with solids volume fractions φ v between 6 and 47%, and particle Reynolds numbers Re p between 0.105 and 0.529. Over the last few decades, research on the rheology of suspensions has advanced through both experimental and computational studies. Brady and Bossis (1985) used Stokesian dynamics to investigate the apparent viscosity (the ratio of the effective viscosity over the viscosity of the suspending fluid) of concentrated suspensions. Jogun and Zukoski (1996) conducted experiments with plate-like particles suspended inside a basic solution to study its rheological behaviour (the yielding type of response). A review article by Stickel and Powell (2005) also discusses the rheology of dense suspensions with more emphasis on microstructure and total fluid stresses. The non-Newtonian behaviour of dense suspensions, such as normal-stress differences and shearinduced migration, has been discussed by Guazzelli (2017) and co-workers (Simon et al., 2015). By coupling the Lattice Boltzmann Method (LBM) with a hybrid Immersed Boundary Method (IBM) and a bounce-back scheme, Lorenz et al. (2018) demonstrated the continuous and dis-2 J o u r n a l P r e -p r o o f Journal Pre-proof J o u r n a l P r e -p r o o f Journal Pre-proof Reynolds number typically of O(10 −1 ), and the flow is laminar. The carrier liquid phase is Newtonian with kinematic viscosity ν. We model the suspensions as consisting of monodisperse rigid spheres that are 300 micron in diameter, which is typical for the slurries we are interested in. 5 J o u r n a l P r e -p r o o f Journal Pre-proof J o u r n a l P r e -p r o o f Journal Pre-proof c for φ v = 10, 33, 40, and 47%. With an increase in φ v , for a fixed h * c the average cluster size 27 J o u r n a l P r e -p r o o f Journal Pre-proof J o u r n a l P r e -p r o o f Journal Pre-proof J o u r n a l P r e -p r o o f Journal Pre-proof J Bergenholtz, J F Brady, and M Vicic. The non-Newtonian rheology of dilute colloidal suspensions. . Local transient rheological behavior of concentrated suspensions. Journal of Rheology, 55(4):835-854, 2011. 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A Sierou and J F Brady. Rheology and microstructure in concentrated noncolloidal suspensions. of dense suspensions of noncolloidal spheres in yield-stress fluids. Journal of Fluid Mechanics, 776, 2015. S Srinivasan, H.E.A Van den Akker, and O Shardt. Shear thickening and history-dependent rheology of monodisperse suspensions with finite inertia via an immersed boundary lattice Boltzmann method. A Ten Cate, J J Derksen, L M Portela, and H E A Van den Akker. Fully resolved simulations of colliding monodisperse spheres in forced isotropic turbulence. Journal of Fluid Mechanics, 519:233-271, 2004. Y Thorimbert, F Marson, A Parmigiani, B Chopard, and J Lätt. Lattice Boltzmann simulation of dense rigid spherical particle suspensions using immersed boundary method. Computers & Fluids, 166:286-294, 2018. 39 J o u r n a l P r e -p r o o f Journal Pre-proof Highlights: Numerical simulations of granular suspensions exhibit weak shear-thickening. The contribution of tangential lubrication stress to the total stress of the suspension is substantial. Temporal evolution of the suspension viscosity and particle structures follow similar dynamics. Memory effects of both the interstitial liquid and particle structures affect the suspension viscosity. J o u r n a l P r e -p r o o f Journal Pre-proof
doi:10.1016/j.compfluid.2021.105115
fatcat:a7ufnjbezvgo7hxmretoosomaq