OpenFOAM-12/tutorials/multiphaseEuler/wallBoilingPolydisperseTwoGroups/constant/phaseProperties

/*--------------------------------*- C++ -*----------------------------------*\
  =========                 |
  \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox
   \\    /   O peration     | Website:  https://openfoam.org
    \\  /    A nd           | Version:  12
     \\/     M anipulation  |
\*---------------------------------------------------------------------------*/
FoamFile
{
    format      ascii;
    class       dictionary;
    location    "constant";
    object      phaseProperties;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //

type    thermalPhaseChangePopulationBalanceMultiphaseSystem;

phases (gas gas2 liquid);

populationBalances (bubbles);

gas
{
    type            purePhaseModel;

    diameterModel   velocityGroup;

    velocityGroupCoeffs
    {
        populationBalance    bubbles;

        shapeModel  spherical;

        sizeGroups
        (
            {dSph 1.0e-4; }
            {dSph 1.2e-4; }
            {dSph 1.44e-4; }
            {dSph 1.728e-4; }
            {dSph 2.074e-4; }
            {dSph 2.49e-4; }
            {dSph 2.99e-4; }
            {dSph 3.6e-4; }
            {dSph 4.3e-4; }
            {dSph 5.16e-4; }
        );
    }

    residualAlpha   1e-6;
}

gas2
{
    type            purePhaseModel;

    diameterModel   velocityGroup;

    velocityGroupCoeffs
    {
        populationBalance    bubbles;

        shapeModel  spherical;

        sizeGroups
        (
            {dSph 6.19e-4; }
            {dSph 7.43e-4; }
            {dSph 8.92e-4; }
            {dSph 1.07e-3; }
            {dSph 1.28e-3; }
            {dSph 1.54e-3; }
            {dSph 1.85e-3; }
            {dSph 2.22e-3; }
            {dSph 2.67e-3; }
            {dSph 3.19e-3; }
            {dSph 3.85e-3; }
            {dSph 4.6e-3; }
            {dSph 5.52e-3; }
            {dSph 6.62e-3; }
            {dSph 7.95e-3; }
            {dSph 9.54e-3; }
            {dSph 1.14e-2; }
        );
    }

    residualAlpha   1e-6;
}

liquid
{
    type            purePhaseModel;

    diameterModel   none;

    Sc              0.7;

    residualAlpha   1e-6;
}

populationBalanceCoeffs
{
    bubbles
    {
        continuousPhase liquid;

        coalescenceModels
        (
            PrinceBlanch
            {
                turbulence on;
                buoyancy   on;
                laminarShear off;
                C1  0.05;
            }
        );

        binaryBreakupModels
        (
            LehrMilliesMewes
            {}
        );

        breakupModels
        ();

        driftModels
        (
            phaseChange
            {
                interfaces (gas_liquid gas2_liquid);
                dmdtf   thermalPhaseChange:dmdtf;
            }

            densityChange
            {}
        );

        nucleationModels
        (
            wallBoiling
            {
                velocityGroup gas;
            }
        );
    }
}

drag
{
    gas_dispersedIn_liquid
    {
        type            IshiiZuber;
    }

    gas2_dispersedIn_liquid
    {
        type            IshiiZuber;
    }
}

virtualMass
{
    gas_dispersedIn_liquid
    {
        type            constantCoefficient;
        Cvm             0.5;
    }

    gas2_dispersedIn_liquid
    {
        type            constantCoefficient;
        Cvm             0.5;
    }
}

heatTransfer
{
    gas_dispersedIn_liquid_inThe_gas
    {
        type spherical;
    }

    gas2_dispersedIn_liquid_inThe_gas2
    {
        type spherical;
    }

    gas_dispersedIn_liquid_inThe_liquid
    {
        type RanzMarshall;
    }

    gas2_dispersedIn_liquid_inThe_liquid
    {
        type RanzMarshall;
    }
}

lift
{
    gas_dispersedIn_liquid
    {
        type wallDamped;

        lift
        {
            type Tomiyama;
            Cl 0.288;

            aspectRatio
            {
                type constant;
                E0 1;
            }
        }

        wallDamping
        {
            type    cosine;
            Cd      1.0;
            zeroWallDist 0.0002;
        }
    }

    gas2_dispersedIn_liquid
    {
        $gas_dispersedIn_liquid
    }
}

wallLubrication
{
   gas_dispersedIn_liquid
    {
        type            Antal;
        Cw1             -0.01;
        Cw2             0.05;
    }

    gas2_dispersedIn_liquid
    {
        $gas_dispersedIn_liquid
    }
}

turbulentDispersion
{
    gas_dispersedIn_liquid
    {
        type                LopezDeBertodano;
        Ctd                 1.0;
        residualAlpha       1e-3;
    }

    gas2_dispersedIn_liquid
    {
        type                LopezDeBertodano;
        Ctd                 1.0;
        residualAlpha       1e-3;
    }
}

blending
{
    default
    {
        type            continuous;
        phase           liquid;
    }
}

saturationTemperature
{
    gas_liquid
    {
        type            function1;

        function
        {
            type            table;
            format          csv;
            nHeaderLine     1;
            units           ([MPa] [K]);
            columns         (1 0);
            mergeSeparators no;
            file "$FOAM_TUTORIALS/resources/thermoData/wallBoiling-saturation.csv";
            outOfBounds     clamp;
            interpolationScheme linear;
        }
    }

    gas2_liquid
    {
        $gas_liquid
    }
}

surfaceTension
{
    gas_liquid
    {
        type            constant;
        sigma           0.00176574;
    }

    gas2_liquid
    {
        $gas_liquid
    }
}

phaseTransfer
{}

// ************************************************************************* //