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Journal ArticleDOI

Verification of filtered two-fluid models for gas-particle flows in risers

Yesim Igci, +1 more
- 01 Oct 2011 - 
- Vol. 57, Iss: 10, pp 2691-2707
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TLDR
In this paper, the effect of solid boundaries on the closure relationships for filtered two-fluid models for riser flows was probed by filtering the results obtained through highly resolved kinetic theory-based two-fluid model simulations.
Abstract
The effect of solid boundaries on the closure relationships for filtered two-fluid models for riser flows was probed by filtering the results obtained through highly resolved kinetic theory-based two-fluid model simulations. The closures for the filtered drag coefficient and particle phase stress depended not only on particle volume fraction and the filter length but also on the distance from the wall. The wall corrections to the filtered closures are nearly independent of the filter length and particle volume fraction. Simulations of filtered model equations yielded grid length independent solutions when the grid length is � half the filter length or smaller. Coarse statistical results obtained by solving the filtered models with different filter lengths were the same and corresponded to those from highly resolved simulations of the kinetic theory model, which was used to construct the filtered models, thus verifying the fidelity of the filtered modeling approach. V V C 2010 American Institute of Chemical Engineers AIChE J, 57: 2691–2707, 2011

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The Future of Pharmaceutical Manufacturing Sciences.

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Journal ArticleDOI

Filtered two‐fluid models of fluidized gas‐particle flows: New constitutive relations

TL;DR: In this paper, constitutive relations for filtered two-fluid models of gas-particle flows are obtained by systematically filtering results generated through highly resolved simulations of a kinetic theory-based TFM.
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Continuum theory for dense gas-solid flow: A state-of-the-art review

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A drag model for filtered Euler–Lagrange simulations of clustered gas–particle suspensions

TL;DR: In this paper, a coarse-grained drag force model for Euler-Lagrange (EL) based simulations of fluidized gas-particle suspensions is presented for the first time in the literature.
Journal ArticleDOI

Constitutive Models for Filtered Two-Fluid Models of Fluidized Gas–Particle Flows

TL;DR: A large number of highly resolved simulations of a kinetic theory based TFM in two- and three-dimensional periodic domains are performed and the results have been captured in the form of correlations that can readily be employed in coarse-grid simulations of gas-particle flows.
References
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Journal ArticleDOI

Frictional–collisional constitutive relations for granular materials, with application to plane shearing

TL;DR: In this article, the authors propose constitutive relations and boundary conditions for plane shear of a cohesionless granular material between infinite horizontal plates, and show that not all the material between the plates participates in shearing and the solutions for the shearing material are coupled to a yield condition for the non-shearing material to give a complete solution of the problem.
Journal ArticleDOI

Wall-layer models for large-eddy simulations

TL;DR: In this article, the authors present three broad classes of approaches: bypassing this region altogether using wall functions, solving a separate set of equations in the nearwall region, weakly coupled to the outer flow, or simulating the near-wall region in a global, Reynolds-averaged, sense.
ReportDOI

MFIX documentation theory guide

TL;DR: This report describes the MFIX (Multiphase Flow with Interphase exchanges) computer model, a general-purpose hydrodynamic model that describes chemical reactions and heat transfer in dense or dilute fluid-solids flows, flows typically occurring in energy conversion and chemical processing reactors.
Journal ArticleDOI

The role of meso-scale structures in rapid gas–solid flows

TL;DR: In this paper, it is shown that the meso-scale structures are too small, and hence too expensive, to be resolved completely in simulation of gas-particle flows in large process vessels.
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