DZ44GBIONA}7`WR})4VI(2V.png
GU0962NTFA1OXF5XX{B5.png
上面是加热壁面，下面全都是多孔区域（孔隙率0.73），然后我产生的液相分布是这样的~ 几乎没有纯气体区域~甚至在固液界面处的液相含量反而高~我已经调过不同的毛细力模型，发现不是毛细力的影响~
现在还可以做的是增大相变系数~但是我相变系数一增大，就会在开始相变的时候发散~

有没有老师可以分析一下可能是哪里导致的问题~

solvers
{
    "alpha.liquid.*"
    {         
        cAlpha          1;
        nAlphaCorr      2;
        nAlphaSubCycles 2;
        MULESCorr       yes;
        nLimiterIter    5;       
        solver          smoothSolver;
        smoother        symGaussSeidel;
        tolerance       1e-7;
        relTol          0;
    }
    rho
    {
        solver           diagonal;
        tolerance        1e-7;
        relTol           0.1;
    }
    rhoFinal
    {
        $rho;
        tolerance        1e-7;
        relTol           0;
    }
    mDotSmearFinal
    {
        solver           PCG;
        tolerance        1e-7;
        preconditioner   DIC;
        relTol           0.00;
        smoother         DIC;
    }
    "(U|T)"
    {
        solver           smoothSolver;
        smoother         symGaussSeidel;
        tolerance        1e-7;
        relTol           0.;
        minIter          15;
        maxIter          50;
    };  
    "(U|T)Final"
    {
        $U;
        tolerance        1e-7;
        relTol           0;
        maxIter          50;
    }
    p
    {
        tolerance        1e-8;
        solver           PCG;
        preconditioner   DIC;
        relTol           0.001;
        smoother         DIC;
    }
    pFinal
    {
        $p;
        tolerance       1e-07;
        relTol          0;
    }    
    "pcorr.*"
    {
        $p_rgh;
        tolerance        1e-9;
        relTol           0;
    };
}
PIMPLE
{
    momentumPredictor   yes;
    nCorrectors         5;
    nNonOrthogonalCorrectors 0;
    pRefCell            0;
    pRefValue           1e5;
}
relaxationFactors
{
    alpha.liquid   0.2;
    U              0.5;
    p              0.5;
}

ddtSchemes
{
    default         Euler;
}
gradSchemes
{
    default         Gauss linear;
}
divSchemes
{
    div(phi,alpha)  Gauss vanLeer01;
    div(phirb,alpha) Gauss vanLeer01;
    //div(phirb,alpha) Gauss interfaceCompression;
    //div(rhoPhi,U)      Gauss vanLeerV;
    //div(rhoPhi,U)      Gauss limitedLinearV 1;
    div(rhoPhi,U)      Gauss linearUpwind;
    div(rhoPhiByEps,U)  Gauss linearUpwind;
    div((mu*dev2(grad(U).T()))) Gauss linear;
    div(((rho*nuEff)*dev2(T(grad(U))))) Gauss linear;
    div(((rho*nu)*dev2(T(grad(U))))) Gauss linear;
    div(rhoCpPhi,T) Gauss vanLeer;
    div((interpolate(cp)*rhoPhi),T) Gauss vanLeer;
}
laplacianSchemes
{
    default         Gauss linear corrected;
}
interpolationSchemes
{
    default         linear;
}
snGradSchemes
{
    default         corrected;
}

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