Files
OpenFOAM-12/tutorials/multiphase/multiphaseEulerFoam/laminar/titaniaSynthesis/constant/phaseProperties
Will Bainbridge 762fb48ddf multiphaseEulerFoam: Use pressureControl
pMin and pMax settings are now available in multiphaseEulerFoam in the
PIMPLE section of the system/fvOptions file. This is consistent with
other compressible solvers. The pMin setting in system/phaseProperties
is no longer read, and it's presence will result in a warning.
2021-03-17 08:42:03 +00:00

217 lines
5.3 KiB
C++

/*--------------------------------*- C++ -*----------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Version: dev
\\/ M anipulation |
\*---------------------------------------------------------------------------*/
FoamFile
{
version 2.0;
format ascii;
class dictionary;
location "constant";
object phaseProperties;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
type populationBalanceMultiphaseSystem;
phases (particles vapor);
populationBalances (aggregates);
particles
{
type multiComponentPhaseModel;
diameterModel velocityGroup;
velocityGroupCoeffs
{
populationBalance aggregates;
shapeModel fractal;
fractalCoeffs
{
sinteringModel KochFriedlander;
KochFriedlanderCoeffs
{
Cs 8.3e24;
n 4.0;
m 1.0;
Ta 3700.0;
}
}
sizeGroups
(
f01{dSph 4.000E-10; value 1.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f02{dSph 5.769E-10; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f03{dSph 8.320E-10; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f04{dSph 1.200E-09; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f05{dSph 1.731E-09; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f06{dSph 2.496E-09; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f07{dSph 3.600E-09; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f08{dSph 5.192E-09; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f09{dSph 7.488E-09; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f10{dSph 1.080E-08; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f11{dSph 1.558E-08; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f12{dSph 2.246E-08; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f13{dSph 3.240E-08; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f14{dSph 4.673E-08; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f15{dSph 6.739E-08; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f16{dSph 9.720E-08; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f17{dSph 1.402E-07; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f18{dSph 2.022E-07; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f19{dSph 2.916E-07; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f20{dSph 4.206E-07; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f21{dSph 6.066E-07; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f22{dSph 8.748E-07; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f23{dSph 1.262E-06; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f24{dSph 1.820E-06; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f25{dSph 2.624E-06; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f26{dSph 3.785E-06; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f27{dSph 5.459E-06; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f28{dSph 7.873E-06; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
f29{dSph 1.136E-05; value 0.0; kappa 1.5E+10; Df 1.8; alphaC 1;}
);
}
residualAlpha 1e-15;
}
vapor
{
type reactingPhaseModel;
diameterModel constant;
constantCoeffs
{
d 1;
}
residualAlpha 1e-5;
}
populationBalanceCoeffs
{
aggregates
{
continuousPhase vapor;
coalescenceModels
(
DahnekeInterpolation
{
sigma 340e-12;
}
);
binaryBreakupModels
();
breakupModels
();
driftModels
();
nucleationModels
(
reactionDriven
{
nucleationDiameter 4E-10;
velocityGroup particles;
reactingPhase vapor;
dmdtf phaseTransfer:dmidtf;
specie TiO2;
}
);
}
}
blending
{
default
{
type none;
continuousPhase vapor;
}
}
interfaceCompression
();
surfaceTension
();
aspectRatio
();
drag
(
(particles in vapor)
{
type timeScaleFiltered;
minRelaxTime 1e-4;
dragModel
{
type aerosolDrag;
sigma 340e-12;
swarmCorrection
{
type none;
}
}
}
);
virtualMass
();
heatTransfer
(
(particles in vapor)
{
type timeScaleFiltered;
minRelaxTime 1e-4;
heatTransferModel
{
type constantNu;
Nu 1;
}
}
);
phaseTransfer
(
(particles in vapor)
{
type reactionDriven;
reactingPhase vapor;
targetPhase particles;
species (TiO2);
}
);
lift
();
wallLubrication
();
turbulentDispersion
();
interfaceCompression
();
// ************************************************************************* //