Computational fluid dynamics of dispersed two-phase flows at high phase fractions

By H. Rusche. 2003

1,110 citations recorded by the source corpus.

View Paper: https://www.semanticscholar.org/paper/1c6cf27039a7cd37229625e7974eafe4138c855d

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Citations in the corpus

Benchmark numerical simulations of segmented two-phase flows in microchannels using the Volume of Fluid method (2013, methodology): “The PISO (pressure-implicit with splitting of operators) scheme is applied for pressure–velocity coupling [41].”
Realistic wave generation and active wave absorption for Navier–Stokes models: Application to OpenFOAM® (2013, background): “For further reference regarding the governing equations see Rusche (2002).”
Modelling two-phase flow in porous media at the pore scale using the volume-of-fluid method (2012, methodology): “where f 0 1⁄4 qgþ fc rpc; ð3Þ u is the velocity vector, p is the total pressure, r T 1⁄4 r ðlruÞ þ ru rl is the viscous force [40], qg is the gravity force and fc is the capillary force, as defined in Eq.”
Challenges in modeling unstable two‐phase flow experiments in porous micromodels (2014, methodology): “…is used here [OpenFOAM, 2011], the advection equation reads @a @t 1r auð Þ1r a 12að Þurð Þ50; (10) where the last term is an artificial compression term used to limit numerical diffusion (ur is a suitable compression velocity [see, e.g., OpenFOAM, 2011; Rusche, 2003; Ferrari and Lunati, 2013]).”
Direct simulations of two-phase flow on micro-CT images of porous media and upscaling of pore-scale forces (2014, background): “For the case of incompressible two-phase flow $ T can be written as (see [50] for the derivation):”
A moving mesh finite volume interface tracking method for surface tension dominated interfacial fluid flow (2012, methodology): “Velocity and acceleration of the moving coordinate system are calculated using the procedure proposed by Rusche [54] in such a way to keep the bubble centre at the origin of the moving coordinate system.”
Wall shear stress from jetting cavitation bubbles (2018, unknown): “U r is the relative velocity between two phases, which helps to ensure a sharp interface (Rusche 2003).”
Extended CFD–DEM for free‐surface flow with multi‐size granules (2016, methodology): “Compared with the conventional VOF method [10, 23], the presence of αf in the temporal derivative term of Equation (8) leads to additional decomposed temporal terms:”