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OpenFOAM-6/tutorials/multiphase/twoPhaseEulerFoam/RAS/bubbleColumn/constant/phaseProperties
Will Bainbridge 85a9e17dd5 reactingEulerFoam: Added phase transfer structure
An additional layer has been added into the phase system hierarchy which
facilitates the application of phase transfer modelling. These are
models which exchange mass between phases without the thermal coupling
that would be required to represent phase change. They can be thought of
as representation changes; e.g., between two phases representing
different droplet sizes of the same physical fluid.

To facilitate this, the heat transfer phase systems have been modified
and renamed and now both support mass transfer. The two sided version
is only required for derivations which support phase change.

The following changes to case settings have been made:

- The simplest instantiated phase systems have been renamed to
basicTwoPhaseSystem and basicMultiphaseSystem. The
heatAndMomentumTransfer*System entries in constant/phaseProperties files
will need updating accordingly.

- A phaseTransfer sub-model entry will be required in the
constant/phaseProperties file. This can be an empty list.

- The massTransfer switch in thermal phase change cases has been renamed
phaseTransfer, so as not to be confused with the mass transfer models
used by interface composition cases.

This work was supported by Georg Skillas and Zhen Li, at Evonik
2018-04-05 15:11:39 +01:00

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2.7 KiB
C++

/*--------------------------------*- C++ -*----------------------------------*\
| ========= | |
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
| \\ / O peration | Version: dev |
| \\ / A nd | Web: www.OpenFOAM.org |
| \\/ M anipulation | |
\*---------------------------------------------------------------------------*/
FoamFile
{
version 2.0;
format ascii;
class dictionary;
location "constant";
object phaseProperties;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
phases (air water);
air
{
diameterModel isothermal;
isothermalCoeffs
{
d0 3e-3;
p0 1e5;
}
residualAlpha 1e-6;
}
water
{
diameterModel constant;
constantCoeffs
{
d 1e-4;
}
residualAlpha 1e-6;
}
blending
{
default
{
type linear;
maxFullyDispersedAlpha.air 0.3;
maxPartlyDispersedAlpha.air 0.5;
maxFullyDispersedAlpha.water 0.3;
maxPartlyDispersedAlpha.water 0.5;
}
}
sigma
(
(air and water) 0.07
);
aspectRatio
(
(air in water)
{
type constant;
E0 1.0;
}
(water in air)
{
type constant;
E0 1.0;
}
);
drag
(
(air in water)
{
type SchillerNaumann;
residualRe 1e-3;
swarmCorrection
{
type none;
}
}
(water in air)
{
type SchillerNaumann;
residualRe 1e-3;
swarmCorrection
{
type none;
}
}
(air and water)
{
type segregated;
m 0.5;
n 8;
swarmCorrection
{
type none;
}
}
);
virtualMass
(
(air in water)
{
type constantCoefficient;
Cvm 0.5;
}
(water in air)
{
type constantCoefficient;
Cvm 0.5;
}
);
heatTransfer
(
(air in water)
{
type RanzMarshall;
residualAlpha 1e-4;
}
(water in air)
{
type RanzMarshall;
residualAlpha 1e-4;
}
);
phaseTransfer
(
);
lift
(
);
wallLubrication
(
);
turbulentDispersion
(
);
// Minimum allowable pressure
pMin 10000;
// ************************************************************************* //