openfoam/tutorials/multiphase/reactingTwoPhaseEulerFoam/RAS/bubbleColumnEvaporatingReacting/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    interfaceCompositionPhaseChangeTwoPhaseSystem;

phases (gas liquid);

gas
{
    type            reactingPhaseModel;
    diameterModel   isothermal;
    isothermalCoeffs
    {
        d0              3e-3;
        p0              1e5;
    }
    Sc              0.7;

    residualAlpha   1e-6;
}

liquid
{
    type            purePhaseModel;
    diameterModel   constant;
    constantCoeffs
    {
        d               1e-4;
    }

    residualAlpha   1e-6;
}

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

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

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

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

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
(
    (gas in liquid)
    {
        type Saturated;
        species ( H2O );
        Le 1.0;
        saturationPressure
        {
            type ArdenBuck;
        }
    }
);

heatTransfer.gas
(
    (gas in liquid)
    {
        type spherical;
        residualAlpha 1e-4;
    }

    (liquid in gas)
    {
        type RanzMarshall;
        residualAlpha 1e-4;
    }
);

heatTransfer.liquid
(
    (gas in liquid)
    {
        type RanzMarshall;
        residualAlpha 1e-4;
    }

    (liquid in gas)
    {
        type spherical;
        residualAlpha 1e-4;
    }
);

massTransfer.gas
(
    (gas in liquid)
    {
        type spherical;
        Le 1.0;
    }

    (liquid in gas)
    {
        type Frossling;
        Le 1.0;
    }
);

massTransfer.liquid
(
);

lift
(
);

wallLubrication
(
);

turbulentDispersion
(
);

// Minimum allowable pressure
pMin            10000;


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