{ word alphaScheme("div(phi,alpha)"); word alpharScheme("div(phirb,alpha)"); surfaceScalarField phir("phir", phic*interface.nHatf()); for (int gCorr=0; gCorr > vDotAlphal = twoPhaseProperties->vDotAlphal(); const volScalarField& vDotcAlphal = vDotAlphal[0](); const volScalarField& vDotvAlphal = vDotAlphal[1](); volScalarField Sp ( IOobject ( "Sp", runTime.timeName(), mesh ), vDotvAlphal - vDotcAlphal ); volScalarField Su ( IOobject ( "Su", runTime.timeName(), mesh ), // Divergence term is handled explicitly to be // consistent with the explicit transport solution divU*alpha1 + vDotcAlphal ); //MULES::explicitSolve(alpha1, phi, phiAlpha, 1, 0); //MULES::explicitSolve(geometricOneField(), alpha1, phi, phiAlpha, Sp, Su, 1, 0); MULES::implicitSolve(geometricOneField(), alpha1, phi, phiAlpha, Sp, Su, 1, 0); rhoPhi += (runTime.deltaT()/totalDeltaT) *(phiAlpha*(rho1 - rho2) + phi*rho2); } Info<< "Liquid phase volume fraction = " << alpha1.weightedAverage(mesh.V()).value() << " Min(alpha1) = " << min(alpha1).value() << " Max(alpha1) = " << max(alpha1).value() << endl; }