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Test case setup parameters

  • Initial temperature in the whole computational domain is set to 35 2
  • Inlet water velocity 36 2 in the pipe region is set to 37 2 having a temperature 38 2
  • For temperature 39 3, the heat transfer boundary conditions at region interfaces are used. Outside patches use externalWallHeatFluxTemperature boundary condition, which supplies a heat flux condition for temperature on an external wall.
  • Example of temperature 39 3 boundary conditions in solid region window on internal patch window-inner-part and external patch window-outer-part is shown below:
    /*--------------------------------*- C++ -*----------------------------------*\
    | =========                 |                                                 |
    | \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox           |
    |  \\    /   O peration     | Version:  dev                                   |
    |   \\  /    A nd           | Web:      www.OpenFOAM.org                      |
    |    \\/     M anipulation  |                                                 |
    \*---------------------------------------------------------------------------*/
    FoamFile
    {
        version     3.0;
        format      ascii;
        class       volScalarField;
        location    "0/window";
        object      T;
    }
    // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
    
    dimensions      [ 0 0 0 1 0 0 0 ];
    
    internalField   uniform 273.15;
    
    boundaryField
    {
        window-inner-part
        {
            type            compressible::turbulentTemperatureCoupledBaffleMixed;
            value           uniform 273.15;
            Tnbr            T;
            kappaMethod     solidThermo;
        }
        window-outer-part
        {
            type            externalWallHeatFluxTemperature;
            mode            coefficient;
            Ta              uniform 273.15;  
            h               uniform 100000.0;
            thicknessLayers ();
            kappaLayers     ();
            kappaMethod     solidThermo;
            value           $internalField;
        }
        window-side
        {
            type            zeroGradient;
            value           uniform 273.15;
        }
    }
    
    // ************************************************************************* //
    
  • Turbulence is not taken into account in this tutorial, therefore the turbulence model is set to laminar
  • Thermophysical properties are different for each region. All solids and fluids have its own molar weight, density, specific heat and thermal conductivity
  • Solver used for this case is chtMultiRegionFoam