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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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CFD simulation of gas–solid bubbling fluidized bed: A new method for adjusting drag law

TL;DR: In this paper, the authors proposed a method for adjusting the Di Felice drag law in a multi-fluid model of FLUENT V6.3.26 (FLUENT, 2007).
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A molecular dynamical study of granular fluids I: the unforced granular gas in two dimensions

TL;DR: In this paper, a numerical study of the dynamics of a collection of disks colliding inelastically in a periodic two-dimensional enclosure is presented, where the velocity distribution functions differ from the classical Maxwell-Boltzmann distribution.
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Granular flow : physical experiments and their implications for microstructural theories

TL;DR: In this paper, positions, velocities and rotations of individual particles obtained from high-speed motion pictures of essentially two-dimensional flows of plastic spheres in an inclined glass-walled chute were used to test critical assumptions of microstructural theories for the flow of granular materials.
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Micromechanical modeling and analysis of different flow regimes in gas fluidization

TL;DR: In this article, the authors investigated the micromechanics of different particle-fluid flow regimes, such as fixed, expanded and fluidized beds, in gas fluidization for group A and B powders.
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Modeling Effects of Operating Conditions on Biomass Fast Pyrolysis in Bubbling Fluidized Bed Reactors

TL;DR: In this paper, a numerical approach that combines a multifluid model and pyrolysis reaction kinetics was applied to simulate the biomass fast pyrotechnics process in a bubbling fluidized-bed reactor.
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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