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Kinetic theories for granular flow: inelastic particles in Couette flow and slightly inelastic particles in a general flowfield

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TLDR
In this paper, the authors studied the flow of an idealized granular material consisting of uniform smooth, but nelastic, spherical particles using statistical methods analogous to those used in the kinetic theory of gases.
Abstract
The flow of an idealized granular material consisting of uniform smooth, but nelastic, spherical particles is studied using statistical methods analogous to those used in the kinetic theory of gases. Two theories are developed: one for the Couette flow of particles having arbitrary coefficients of restitution (inelastic particles) and a second for the general flow of particles with coefficients of restitution near 1 (slightly inelastic particles). The study of inelastic particles in Couette flow follows the method of Savage & Jeffrey (1981) and uses an ad hoc distribution function to describe the collisions between particles. The results of this first analysis are compared with other theories of granular flow, with the Chapman-Enskog dense-gas theory, and with experiments. The theory agrees moderately well with experimental data and it is found that the asymptotic analysis of Jenkins & Savage (1983), which was developed for slightly inelastic particles, surprisingly gives results similar to the first theory even for highly inelastic particles. Therefore the ‘nearly elastic’ approximation is pursued as a second theory using an approach that is closer to the established methods of Chapman-Enskog gas theory. The new approach which determines the collisional distribution functions by a rational approximation scheme, is applicable to general flowfields, not just simple shear. It incorporates kinetic as well as collisional contributions to the constitutive equations for stress and energy flux and is thus appropriate for dilute as well as dense concentrations of solids. When the collisional contributions are dominant, it predicts stresses similar to the first analysis for the simple shear case.

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Modelling of the behaviour of gas–solid two-phase mixtures flowing through packed beds

TL;DR: In this paper, an Eulerian-based two-fluid model coupled with a newly proposed porosity distribution model is used to simulate the flow behavior of gas-solid two-phase mixtures flowing upwards through packed beds.
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CFD modeling the hydrodynamics of binary particle mixture in pseudo-2D bubbling fluidized bed: Effect of model parameters

TL;DR: In this article, the hydrodynamics of binary coal-sand mixture in a pseudo-2D rectangular bubbling fluidized bed (0.385m, 0.005m, and 0.128m) were simulated using the multi-fluid Eulerian model incorporating the kinetic theory of granular flow.
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Modeling and simulation of the influences of particle-particle interactions on dense solid–liquid suspensions in stirred vessels

TL;DR: In this paper, an Eulerian-Eulerian model is used to characterize the suspension dynamics and the role of particle-particle interactions in solid-liquid mixing vessels is studied.
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Comparative CFD modeling of a bubbling bed using a Eulerian–Eulerian two-fluid model (TFM) and a Eulerian-Lagrangian dense discrete phase model (DDPM)

TL;DR: In this article, the numerical performance of a two-fluid model (TFM) and a dense discrete phase model (DDPM) in describing the hydrodynamic behavior of a pilot-scale bubbling bed reactor was compared and compared for the two approaches using two-dimensional (2D) simulations.
References
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Journal ArticleDOI

Equation of State for Nonattracting Rigid Spheres

TL;DR: In this paper, a new equation of state for rigid spheres has been developed from an analysis of the reduced virial series, which possesses superior ability to describe rigid-sphere behavior compared with existing equations.
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Experiments on a Gravity-Free Dispersion of Large Solid Spheres in a Newtonian Fluid under Shear

TL;DR: In this article, a large number of spherical grains of diameter D = 0.13 cm were sheared in Newtonian fluids of varying viscosity (water and a glycerine-water-alcohol mixture) in the annular space between two concentric drums.
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