OpenFOAM-12/tutorials/modules/multiphaseEuler/bubbleColumnEvaporatingDissolving/constant/phaseProperties

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

type    interfaceCompositionPhaseChangeMultiphaseSystem;

phases (gas liquid);

gas
{
    type            multicomponentPhaseModel;
    diameterModel   isothermal;
    isothermalCoeffs
    {
        d0              3e-3;
        p0              1e5;
    }

    residualAlpha   1e-6;
}

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

    residualAlpha   1e-6;
}

blending
{
    default
    {
        type            linear;
        minFullyContinuousAlpha.gas 0.7;
        minPartlyContinuousAlpha.gas 0.3;
        minFullyContinuousAlpha.liquid 0.7;
        minPartlyContinuousAlpha.liquid 0.3;
    }

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

    diffusiveMassTransfer
    {
        $heatTransfer;
    }
}

surfaceTension
{
    gas_liquid
    {
        type            constant;
        sigma           0.07;
    }
}

drag
{
    gas_dispersedIn_liquid
    {
        type            SchillerNaumann;
        residualRe      1e-3;
    }

    liquid_dispersedIn_gas
    {
        type            SchillerNaumann;
        residualRe      1e-3;
    }
}

virtualMass
{
    gas_dispersedIn_liquid
    {
        type            constantCoefficient;
        Cvm             0.5;
    }

    liquid_dispersedIn_gas
    {
        type            constantCoefficient;
        Cvm             0.5;
    }
}

interfaceComposition
{
    gas_liquid_inThe_gas
    {
        type saturated;
        species ( water );
        Le 1.0;
        pSat ArdenBuck;
    }

    gas_liquid_inThe_liquid
    {
        type Henry;
        species ( air );
        k ( 1.492e-2 );
        Le 1.0;
    }
}

heatTransfer
{
    gas_dispersedIn_liquid_inThe_gas
    {
        type spherical;
        residualAlpha 1e-4;
    }

    liquid_dispersedIn_gas_inThe_gas
    {
        type RanzMarshall;
        residualAlpha 1e-4;
    }

    gas_dispersedIn_liquid_inThe_liquid
    {
        type RanzMarshall;
        residualAlpha 1e-4;
    }

    liquid_dispersedIn_gas_inThe_liquid
    {
        type spherical;
        residualAlpha 1e-4;
    }
}

diffusiveMassTransfer
{
    gas_dispersedIn_liquid_inThe_gas
    {
        type spherical;
    }

    liquid_dispersedIn_gas_inThe_gas
    {
        type Frossling;
        Le 1.0;
    }

    gas_dispersedIn_liquid_inThe_liquid
    {
        type Frossling;
        Le 1.0;
    }

    liquid_dispersedIn_gas_inThe_liquid
    {
        type spherical;
    }
}

phaseTransfer
{}

lift
{}

wallLubrication
{}

turbulentDispersion
{}

interfaceCompression
{}

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