openfoam/tutorials/multiphase/reactingTwoPhaseEulerFoam/RAS/wallBoilingIATE/constant/phaseProperties

/*--------------------------------*- 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;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //

type    thermalPhaseChangeTwoPhaseSystem;

phases (gas liquid);

volatile    "water";

massTransfer on;

gas
{
    type            multiComponentPhaseModel;
    diameterModel   IATE;

    IATECoeffs
    {
        dMax 1e-2;
        dMin 1e-4;
        residualAlpha 1e-4;

        sources
        (
            wakeEntrainmentCoalescence
            {
                Cwe         0.002;
            }

            randomCoalescence
            {
                Crc         0.04;
                C           3;
                alphaMax    0.75;
            }

            turbulentBreakUp
            {
                Cti         0.085;
                WeCr        6;
            }

            wallBoiling
            {}
        );
    }

    constantCoeffs
    {
        d               0.00045;
    }

    isothermalCoeffs
    {
        d0               0.00045;
        p0              1e5;
    }

    Sc              0.7;

    residualAlpha   1e-4;
}

liquid
{
    type            multiComponentPhaseModel;
    diameterModel   constant;
    constantCoeffs
    {
        d               0.00045;
    }
    Sc              0.7;

    residualAlpha   1e-4;
}

blending
{
    default
    {
        type            linear;
        continuousPhase liquid;
        minFullyContinuousAlpha.gas 0.7;
        minPartlyContinuousAlpha.gas 0.5;
        minFullyContinuousAlpha.liquid 0.7;
        minPartlyContinuousAlpha.liquid 0.5;
    }

    heatTransfer
    {
        type            linear;
        continuousPhase liquid;
        minFullyContinuousAlpha.gas 1;
        minPartlyContinuousAlpha.gas 0;
        minFullyContinuousAlpha.liquid 1;
        minPartlyContinuousAlpha.liquid 0;
    }

    massTransfer
    {
        type            linear;
        continuousPhase liquid;
        minFullyContinuousAlpha.gas 1;
        minPartlyContinuousAlpha.gas 0;
        minFullyContinuousAlpha.liquid 1;
        minPartlyContinuousAlpha.liquid 0;
    }
}

surfaceTension
(
    (gas and liquid)
    {
        type            constant;
        sigma           0.07;
    }
);

saturationModel
{
    type polynomial;
    C<8>
    (
        308.0422
        0.0015096
        -1.61589e-8
        1.114106e-13
        -4.52216e-19
        1.05192e-24
        -1.2953e-30
        6.5365e-37
    );
};

aspectRatio
(
    (gas in liquid)
    {
        type            constant;
        E0              1.0;
    }

    (liquid in gas)
    {
        type            constant;
        E0              1.0;
    }
);

drag
(
    (gas in liquid)
    {
        type            SchillerNaumann;
        residualRe      1e-3;
        swarmCorrection
        {
            type        none;
        }
    }

    (liquid in gas)
    {
        type            SchillerNaumann;
        residualRe      1e-3;
        swarmCorrection
        {
            type        none;
        }
    }
);

virtualMass
(
    (gas in liquid)
    {
        type            constantCoefficient;
        Cvm             0.5;
    }

    (liquid in gas)
    {
        type            constantCoefficient;
        Cvm             0.5;
    }
);

interfaceComposition
();

heatTransfer.gas
(
    (gas in liquid)
    {
        type spherical;
        residualAlpha 1e-3;
    }

    (liquid in gas)
    {
        type RanzMarshall;
        residualAlpha 1e-3;
    }
);

heatTransfer.liquid
(
    (gas in liquid)
    {
        type RanzMarshall;
        residualAlpha 1e-3;
    }

    (liquid in gas)
    {
        type spherical;
        residualAlpha 1e-3;
    }
);

massTransfer.gas
();

massTransfer.liquid
();

lift
();

wallLubrication
(
    (gas in liquid)
    {
        type            Antal;
        Cw1             -0.01;
        Cw2             0.05;
        Cwc             10.0;
        Cwd             6.8;
        p               1.7;
    }
);

turbulentDispersion
(
    (gas in liquid)
    {
        type                Burns;
        sigma               0.7;
        Ctd                 1.0;
        residualAlpha       1e-3;
    }
);

// Minimum allowable pressure
pMin            10000;


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