2019
DOI: 10.1016/j.compfluid.2019.104293
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A fictitious domain method for particulate flows of arbitrary density ratio

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Cited by 8 publications
(6 citation statements)
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“…Vreman (2015) demonstrated that the non-uniform part of the mean feedback drag force contributed significantly to particle-induced turbulence attenuation. Xia, Yu & Deng (2019) observed that, at the same settling coefficient, light (bubble) particles attenuated the turbulence in a downward channel flow, where the particles migrated towards the channel centre, whereas light particles enhanced the turbulence in an upward channel, where the particles migrated towards the channel wall. From these observations, it seems that the particle feedback force distributed in the bulk region suppresses the self-generation of large-scale vortices in the channel flow.…”
Section: Vortex Structurementioning
confidence: 95%
“…Vreman (2015) demonstrated that the non-uniform part of the mean feedback drag force contributed significantly to particle-induced turbulence attenuation. Xia, Yu & Deng (2019) observed that, at the same settling coefficient, light (bubble) particles attenuated the turbulence in a downward channel flow, where the particles migrated towards the channel centre, whereas light particles enhanced the turbulence in an upward channel, where the particles migrated towards the channel wall. From these observations, it seems that the particle feedback force distributed in the bulk region suppresses the self-generation of large-scale vortices in the channel flow.…”
Section: Vortex Structurementioning
confidence: 95%
“…Considering single-phase flow and ignoring the influence of solid phase on continuous phase flow, continuity and momentum can be written as Eqs ( 1 ) and ( 2 ) [ 19 ]. ∇ is the vector of Differential operator, p is the pressure, ρ is the fluid density, u is the velocity, g is the Gravitational acceleration, τviscous shear stress can be defined by Formula ( 3 ) [ 20 ]。 By substituting the viscous shear τ in a Newtonian fluid from Eq (3) into Eq ( 1 ) and considering an incompressible Newtonian fluid (where the shear deformation of the fluid under stress is linear), Eq ( 4 ) can be obtained. As the Reynolds number increases (i.e., the ratio of inertial to viscous forces) the flow state changes from creep (the convective term in the momentum equation can be ignored), to laminar, to transitional, and finally to turbulent.…”
Section: Methodsmentioning
confidence: 99%
“…In [5], a fictitious domain method with Distributed Lagrange Multipliers for simulating two-dimensional (hereinafter 2D) unsteady shear-thinning non-newtonian incompressible flow in a single-screw and twin-screw extruder is developed. The issues of flow motion with an arbitrary density of particles are considered in [6].…”
Section: Literature Review and Problem Statementmentioning
confidence: 99%
“…In [4][5][6], the authors successfully applied the fictitious domain method for numerical simulation of incompressible fluids in different areas, carried out theoretical and numerical analyses, and also used the finite element method. It is important to note that the finite element method won't always work for parallel computing.…”
Section: Literature Review and Problem Statementmentioning
confidence: 99%
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