Example #1
0
def _pEqn( runTime, mesh, UEqn, thermo, p, psi, U, rho, phi, DpDt, g, initialMass, totalVolume, corr, nCorr, nNonOrthCorr, cumulativeContErr ): 
    closedVolume = p.needReference()
    rho.ext_assign( thermo.rho() )

    # Thermodynamic density needs to be updated by psi*d(p) after the
    # pressure solution - done in 2 parts. Part 1:
    thermo.rho().ext_assign( thermo.rho() - psi * p )
    
    rUA = 1.0/UEqn.A()
    from Foam.OpenFOAM import word
    from Foam.finiteVolume import surfaceScalarField
    from Foam import fvc
    rhorUAf = surfaceScalarField( word( "(rho*(1|A(U)))" ), fvc.interpolate( rho * rUA ) )

    U.ext_assign( rUA * UEqn.H() )

    phiU = fvc.interpolate( rho ) * ( (fvc.interpolate( U ) & mesh.Sf() ) + fvc.ddtPhiCorr( rUA, rho, U, phi ) ) 

    phi.ext_assign( phiU + rhorUAf * fvc.interpolate( rho ) * (g & mesh.Sf() ) )
    
    for nonOrth in range( nNonOrthCorr+1 ):
        
        from Foam import fvm
        from Foam.finiteVolume import correction
        pEqn = fvc.ddt( rho ) + psi * correction( fvm.ddt( p ) ) + fvc.div( phi ) - fvm.laplacian( rhorUAf, p )
        
        if corr == nCorr-1  and nonOrth == nNonOrthCorr:
           pEqn.solve( mesh.solver( word( str( p.name() ) + "Final" ) ) )
           pass
        else:
           pEqn.solve( mesh.solver( p.name() ) )
           pass
        if nonOrth == nNonOrthCorr:
           phi.ext_assign( phi + pEqn.flux() )
           pass

    # Second part of thermodynamic density update
    thermo.rho().ext_assign( thermo.rho() + psi * p )

    U.ext_assign( U + rUA * fvc.reconstruct( ( phi - phiU ) / rhorUAf ) )
    U.correctBoundaryConditions()
    
    DpDt.ext_assign( fvc.DDt( surfaceScalarField( word( "phiU" ), phi / fvc.interpolate( rho ) ), p ) )
    
    from Foam.finiteVolume.cfdTools.compressible import rhoEqn  
    rhoEqn( rho, phi )
    
    from Foam.finiteVolume.cfdTools.compressible import compressibleContinuityErrs
    cumulativeContErr = compressibleContinuityErrs( rho, thermo, cumulativeContErr )

    # For closed-volume cases adjust the pressure and density levels
    # to obey overall mass continuity
    if closedVolume:
       p.ext_assign( p + ( initialMass - fvc.domainIntegrate( psi * p ) ) / fvc.domainIntegrate( psi ) )
       thermo.rho().ext_assign(  psi * p )
       rho.ext_assign( rho + ( initialMass - fvc.domainIntegrate( rho ) ) / totalVolume )
       pass

    return cumulativeContErr
Example #2
0
def fun_pEqn( i, mesh, p, rho, turb, thermo, thermoFluid, K, UEqn, U, phi, psi, DpDt, initialMass, p_rgh, gh, ghf, \
              nNonOrthCorr, oCorr, nOuterCorr, corr, nCorr, cumulativeContErr ) :
    
    closedVolume = p_rgh.needReference()

    rho.ext_assign( thermo.rho() )
    
    rUA = 1.0 / UEqn.A()
    
    from Foam import fvc
    from Foam.OpenFOAM import word 
    from Foam.finiteVolume import surfaceScalarField
    rhorUAf = surfaceScalarField( word( "(rho*(1|A(U)))" ) , fvc.interpolate( rho * rUA ) )

    U.ext_assign( rUA * UEqn.H() ) 

    from Foam import fvc

    phiU = ( fvc.interpolate( rho ) *
                 (  ( fvc.interpolate( U ) & mesh.Sf() ) +
                      fvc.ddtPhiCorr( rUA, rho, U, phi ) ) )
    phi.ext_assign( phiU - rhorUAf * ghf * fvc.snGrad( rho ) * mesh.magSf() )
    from Foam import fvm
    for nonOrth in range ( nNonOrthCorr + 1 ):
        p_rghEqn = ( fvm.ddt( psi, p_rgh) + fvc.ddt( psi, rho ) * gh + fvc.div( phi ) - fvm.laplacian( rhorUAf, p_rgh ) )
        p_rghEqn.solve( mesh.solver( p_rgh.select( ( oCorr == nOuterCorr-1 and corr == ( nCorr-1 ) and nonOrth == nNonOrthCorr ) ) ) )
        
        if nonOrth == nNonOrthCorr :
            phi.ext_assign( phi + p_rghEqn.flux() )
            pass
        pass
    
    # Correct velocity field
    U.ext_assign( U + rUA * fvc.reconstruct( ( phi - phiU ) / rhorUAf ) )
    U.correctBoundaryConditions()
    
    p.ext_assign( p_rgh + rho * gh )

    #Update pressure substantive derivative
    DpDt.ext_assign( fvc.DDt( surfaceScalarField( word( "phiU" ), phi / fvc.interpolate( rho ) ), p ) )
    
    # Solve continuity
    from Foam.finiteVolume.cfdTools.compressible import rhoEqn
    rhoEqn( rho, phi )   
    
    # Update continuity errors
    cumulativeContErr = compressibleContinuityErrors( i, mesh, rho, thermo, cumulativeContErr )
    
    # For closed-volume cases adjust the pressure and density levels
    # to obey overall mass continuity
    if closedVolume :
       p.ext_assign( p + ( initialMass - fvc.domainIntegrate( psi * p ) ) / fvc.domainIntegrate( psi ) )
       rho.ext_assign( thermo.rho() )
       p_rgh.ext_assign( p - rho * gh )
       pass
    #Update thermal conductivity
    K.ext_assign( thermoFluid[ i ].Cp() * turb.alphaEff() )
        
    return cumulativeContErr
Example #3
0
def fun_pEqn( mesh, p, rho, psi, p_rgh, U, phi, ghf, gh, DpDt, UEqn, thermo, nNonOrthCorr, corr, nCorr, finalIter, cumulativeContErr ):
    
    rho.ext_assign( thermo.rho() )

    # Thermodynamic density needs to be updated by psi*d(p) after the
    # pressure solution - done in 2 parts. Part 1:
    thermo.rho().ext_assign( thermo.rho() - psi * p_rgh )

    rUA = 1.0 / UEqn.A()
    from Foam.finiteVolume import surfaceScalarField
    from Foam.OpenFOAM import word
    from Foam import fvc
    rhorUAf = surfaceScalarField( word( "(rho*(1|A(U)))" ), fvc.interpolate( rho * rUA ) )

    U.ext_assign( rUA*UEqn.H() )

    phi.ext_assign( fvc.interpolate( rho ) * ( ( fvc.interpolate( U ) & mesh.Sf() ) + fvc.ddtPhiCorr( rUA, rho, U, phi ) ) )

    buoyancyPhi = -rhorUAf * ghf * fvc.snGrad( rho ) * mesh.magSf()
    phi.ext_assign( phi + buoyancyPhi )
    
    from Foam import fvm
    from Foam.finiteVolume import correction
    for nonOrth in range( nNonOrthCorr +1 ):
        p_rghEqn = fvc.ddt( rho ) + psi * correction( fvm.ddt( p_rgh ) ) + fvc.div( phi ) - fvm.laplacian( rhorUAf, p_rgh )

        p_rghEqn.solve( mesh.solver( p_rgh.select( ( finalIter and corr == nCorr-1 and nonOrth == nNonOrthCorr ) ) ) )

        if nonOrth == nNonOrthCorr:
            # Calculate the conservative fluxes
            phi.ext_assign( phi + p_rghEqn.flux() )

            # Explicitly relax pressure for momentum corrector
            p_rgh.relax()

            # Correct the momentum source with the pressure gradient flux
            # calculated from the relaxed pressure
            U.ext_assign( U + rUA * fvc.reconstruct( ( buoyancyPhi + p_rghEqn.flux() ) / rhorUAf ) )
            U.correctBoundaryConditions()
            pass

    p.ext_assign( p_rgh + rho * gh )

    # Second part of thermodynamic density update
    thermo.rho().ext_assign( thermo.rho() + psi * p_rgh )

    DpDt.ext_assign( fvc.DDt( surfaceScalarField( word( "phiU" ), phi / fvc.interpolate( rho ) ), p ) )

    from Foam.finiteVolume.cfdTools.compressible import rhoEqn  
    rhoEqn( rho, phi )
    
    from Foam.finiteVolume.cfdTools.compressible import compressibleContinuityErrs
    cumulativeContErr = compressibleContinuityErrs( rho, thermo, cumulativeContErr )

    return cumulativeContErr
Example #4
0
def fun_pdEqn( corr, nCorr, nNonOrthCorr, closedVolume, pd, pRef, rho, psi, rUA, gh, phi ):
    
    closedVolume = pd.needReference()

    for nonOrth in range( nNonOrthCorr + 1):
        from Foam import fvc, fvm
        pdEqn =  fvm.ddt( psi, pd ) + fvc.ddt( psi ) * pRef + fvc.ddt(psi, rho) * gh + fvc.div( phi ) - fvm.laplacian( rho * rUA, pd )
        
        pdEqn.solve()
        if corr == nCorr-1 and nonOrth == nNonOrthCorr :
           from Foam.OpenFOAM import word 
           pdEqn.solve( pd.mesh().solver( word( str( pd.name() ) + "Final" ) ) )
           pass
        else:
           pdEqn.solve( pd.mesh().solver( pd.name() ) )
           pass

        if nonOrth == nNonOrthCorr:
           phi.ext_assign(phi + pdEqn.flux() )
    
    return pdEqn, closedVolume
Example #5
0
def fun_pEqn( i, mesh, p, rho, turb, thermo, thermoFluid, K, UEqn, U, phi, psi, DpDt, initialMass, p_rgh, gh, ghf, \
              nNonOrthCorr, oCorr, nOuterCorr, corr, nCorr, cumulativeContErr ) :

    closedVolume = p_rgh.needReference()

    rho.ext_assign(thermo.rho())

    rUA = 1.0 / UEqn.A()

    from Foam import fvc
    from Foam.OpenFOAM import word
    from Foam.finiteVolume import surfaceScalarField
    rhorUAf = surfaceScalarField(word("(rho*(1|A(U)))"),
                                 fvc.interpolate(rho * rUA))

    U.ext_assign(rUA * UEqn.H())

    from Foam import fvc

    phiU = (fvc.interpolate(rho) * (
        (fvc.interpolate(U) & mesh.Sf()) + fvc.ddtPhiCorr(rUA, rho, U, phi)))
    phi.ext_assign(phiU - rhorUAf * ghf * fvc.snGrad(rho) * mesh.magSf())
    from Foam import fvm
    for nonOrth in range(nNonOrthCorr + 1):
        p_rghEqn = (fvm.ddt(psi, p_rgh) + fvc.ddt(psi, rho) * gh +
                    fvc.div(phi) - fvm.laplacian(rhorUAf, p_rgh))
        p_rghEqn.solve(
            mesh.solver(
                p_rgh.select((oCorr == nOuterCorr - 1 and corr == (nCorr - 1)
                              and nonOrth == nNonOrthCorr))))

        if nonOrth == nNonOrthCorr:
            phi.ext_assign(phi + p_rghEqn.flux())
            pass
        pass

    # Correct velocity field
    U.ext_assign(U + rUA * fvc.reconstruct((phi - phiU) / rhorUAf))
    U.correctBoundaryConditions()

    p.ext_assign(p_rgh + rho * gh)

    #Update pressure substantive derivative
    DpDt.ext_assign(
        fvc.DDt(surfaceScalarField(word("phiU"), phi / fvc.interpolate(rho)),
                p))

    # Solve continuity
    from Foam.finiteVolume.cfdTools.compressible import rhoEqn
    rhoEqn(rho, phi)

    # Update continuity errors
    cumulativeContErr = compressibleContinuityErrors(i, mesh, rho, thermo,
                                                     cumulativeContErr)

    # For closed-volume cases adjust the pressure and density levels
    # to obey overall mass continuity
    if closedVolume:
        p.ext_assign(p + (initialMass - fvc.domainIntegrate(psi * p)) /
                     fvc.domainIntegrate(psi))
        rho.ext_assign(thermo.rho())
        p_rgh.ext_assign(p - rho * gh)
        pass
    #Update thermal conductivity
    K.ext_assign(thermoFluid[i].Cp() * turb.alphaEff())

    return cumulativeContErr
Example #6
0
def main_standalone( argc, argv ):

    from Foam.OpenFOAM.include import setRootCase
    args = setRootCase( argc, argv )

    from Foam.OpenFOAM.include import createTime
    runTime = createTime( args )

    from Foam.OpenFOAM.include import createMesh
    mesh = createMesh( runTime )
    
    thermo, p, e, T, psi, mu, U, pbf, rhoBoundaryTypes, rho, rhoU, rhoE, pos, neg, inviscid = _createFields( runTime, mesh )
    
    thermophysicalProperties, Pr = readThermophysicalProperties( runTime, mesh )
    
    from Foam.finiteVolume.cfdTools.general.include import readTimeControls
    adjustTimeStep, maxCo, maxDeltaT = readTimeControls( runTime )
    
    fluxScheme = readFluxScheme( mesh )
    
    from Foam.OpenFOAM import dimensionedScalar, dimVolume, dimTime, word
    v_zero = dimensionedScalar( word( "v_zero" ) ,dimVolume/dimTime, 0.0)
    
    from Foam.OpenFOAM import ext_Info, nl
    ext_Info() << "\nStarting time loop\n" << nl
    
    while runTime.run() :
        # --- upwind interpolation of primitive fields on faces
        from Foam import fvc
        rho_pos = fvc.interpolate( rho, pos, word( "reconstruct(rho)" ) )
        rho_neg = fvc.interpolate( rho, neg, word( "reconstruct(rho)" ) )
        
        rhoU_pos = fvc.interpolate( rhoU, pos, word( "reconstruct(U)" ) )
        rhoU_neg = fvc.interpolate( rhoU, neg, word( "reconstruct(U)" ) )
        
        rPsi = 1.0 / psi
        rPsi_pos = fvc.interpolate( rPsi, pos, word( "reconstruct(T)" ) )
        rPsi_neg = fvc.interpolate( rPsi, neg, word( "reconstruct(T)" ) )
        
        e_pos = fvc.interpolate( e, pos, word( "reconstruct(T)" ) )
        e_neg = fvc.interpolate( e, neg, word( "reconstruct(T)" ) )
        
        U_pos = rhoU_pos / rho_pos
        U_neg = rhoU_neg / rho_neg

        p_pos = rho_pos * rPsi_pos
        p_neg = rho_neg * rPsi_neg

        phiv_pos = U_pos & mesh.Sf()
        phiv_neg = U_neg & mesh.Sf()
        
        c = ( thermo.Cp() / thermo.Cv() * rPsi ).sqrt()
        cSf_pos = fvc.interpolate( c, pos, word( "reconstruct(T)" ) ) * mesh.magSf()
        cSf_neg = fvc.interpolate( c, neg, word( "reconstruct(T)" ) ) * mesh.magSf()
        
        ap = ( phiv_pos + cSf_pos ).ext_max( phiv_neg + cSf_neg ).ext_max( v_zero )
        am = ( phiv_pos - cSf_pos ).ext_min( phiv_neg - cSf_neg ).ext_min( v_zero )

        a_pos = ap / ( ap - am )
        
        from Foam.finiteVolume import surfaceScalarField
        amaxSf = surfaceScalarField( word( "amaxSf" ), am.mag().ext_max( ap.mag() ) )
        
        CoNum, meanCoNum = compressibleCourantNo( mesh, amaxSf, runTime )
        
        from Foam.finiteVolume.cfdTools.general.include import readTimeControls
        adjustTimeStep, maxCo, maxDeltaT = readTimeControls( runTime )
        
        from Foam.finiteVolume.cfdTools.general.include import setDeltaT
        runTime = setDeltaT( runTime, adjustTimeStep, maxCo, maxDeltaT, CoNum )
        
        runTime.increment()
        
        ext_Info() << "Time = " << runTime.timeName() << nl << nl
        
        aSf = am * a_pos

        if str( fluxScheme ) == "Tadmor":
           aSf.ext_assign( -0.5 * amaxSf )
           a_pos.ext_assign( 0.5 )
           pass
        
        a_neg = 1.0 - a_pos
        
        phiv_pos *= a_pos
        phiv_neg *= a_neg
        
        aphiv_pos = phiv_pos - aSf
        
        aphiv_neg = phiv_neg + aSf

        phi = None

        phi = surfaceScalarField( word( "phi" ), aphiv_pos * rho_pos + aphiv_neg * rho_neg )

        phiUp = ( aphiv_pos * rhoU_pos + aphiv_neg * rhoU_neg) + ( a_pos * p_pos + a_neg * p_neg ) * mesh.Sf()

        phiEp = aphiv_pos * ( rho_pos * ( e_pos + 0.5*U_pos.magSqr() ) + p_pos ) + aphiv_neg * ( rho_neg * ( e_neg + 0.5 * U_neg.magSqr() ) + p_neg )\
                + aSf * p_pos - aSf * p_neg
        
        from Foam.finiteVolume import volTensorField
        from Foam import fvc
        tauMC = volTensorField( word( "tauMC" ) , mu * fvc.grad(U).T().dev2() ) 
        
        # --- Solve density
        from Foam.finiteVolume import solve
        from Foam import fvm
        solve( fvm.ddt( rho ) + fvc.div( phi ) )
        
        # --- Solve momentum
        solve( fvm.ddt( rhoU ) + fvc.div( phiUp ) )
        
        U.dimensionedInternalField().ext_assign( rhoU.dimensionedInternalField() / rho.dimensionedInternalField() )
        U.correctBoundaryConditions()
        rhoU.ext_boundaryField().ext_assign( rho.ext_boundaryField() * U.ext_boundaryField() )
        
        rhoBydt = rho / runTime.deltaT()
        
        if not inviscid:
           solve( fvm.ddt( rho, U ) - fvc.ddt( rho, U ) - fvm.laplacian( mu, U ) - fvc.div( tauMC ) )
           rhoU.ext_assign( rho * U )
           pass
        
        # --- Solve energy
        sigmaDotU = ( fvc.interpolate( mu ) * mesh.magSf() * fvc.snGrad( U ) + ( mesh.Sf() & fvc.interpolate( tauMC ) ) ) & ( a_pos * U_pos + a_neg * U_neg )

        solve( fvm.ddt( rhoE ) + fvc.div( phiEp ) - fvc.div( sigmaDotU ) )
        
        e.ext_assign( rhoE / rho - 0.5 * U.magSqr() )
        e.correctBoundaryConditions()
        thermo.correct()
        from Foam.finiteVolume import volScalarField
        rhoE.ext_boundaryField().ext_assign( rho.ext_boundaryField() * ( e.ext_boundaryField() + 0.5 * U.ext_boundaryField().magSqr() ) )
        
        if not inviscid:
           k = volScalarField( word( "k" ) , thermo.Cp() * mu / Pr )

           # The initial C++ expression does not work properly, because of
           #  1. the order of expression arguments computation differs with C++
           #solve( fvm.ddt( rho, e ) - fvc.ddt( rho, e ) - fvm.laplacian( thermo.alpha(), e ) \
           #                                             + fvc.laplacian( thermo.alpha(), e ) - fvc.laplacian( k, T ) )

           solve( -fvc.laplacian( k, T ) + ( fvc.laplacian( thermo.alpha(), e ) \
                                         + (- fvm.laplacian( thermo.alpha(), e ) + (- fvc.ddt( rho, e ) + fvm.ddt( rho, e ) ) ) ) )
           
           thermo.correct()
           rhoE.ext_assign( rho * ( e + 0.5 * U.magSqr() ) )
           pass
        
        p.dimensionedInternalField().ext_assign( rho.dimensionedInternalField() / psi.dimensionedInternalField() )
        p.correctBoundaryConditions()
        rho.ext_boundaryField().ext_assign( psi.ext_boundaryField() * p.ext_boundaryField() )
        
        runTime.write()

        ext_Info() << "ExecutionTime = " << runTime.elapsedCpuTime() << " s" << \
              "  ClockTime = " << runTime.elapsedClockTime() << " s" << nl << nl
        
        pass

    ext_Info() << "End\n"

    import os
    return os.EX_OK
Example #7
0
def _pEqn(runTime, mesh, UEqn, thermo, p, psi, U, rho, phi, DpDt, g,
          initialMass, totalVolume, corr, nCorr, nNonOrthCorr,
          cumulativeContErr):
    closedVolume = p.needReference()
    rho.ext_assign(thermo.rho())

    # Thermodynamic density needs to be updated by psi*d(p) after the
    # pressure solution - done in 2 parts. Part 1:
    thermo.rho().ext_assign(thermo.rho() - psi * p)

    rUA = 1.0 / UEqn.A()
    from Foam.OpenFOAM import word
    from Foam.finiteVolume import surfaceScalarField
    from Foam import fvc
    rhorUAf = surfaceScalarField(word("(rho*(1|A(U)))"),
                                 fvc.interpolate(rho * rUA))

    U.ext_assign(rUA * UEqn.H())

    phiU = fvc.interpolate(rho) * (
        (fvc.interpolate(U) & mesh.Sf()) + fvc.ddtPhiCorr(rUA, rho, U, phi))

    phi.ext_assign(phiU + rhorUAf * fvc.interpolate(rho) * (g & mesh.Sf()))

    for nonOrth in range(nNonOrthCorr + 1):

        from Foam import fvm
        from Foam.finiteVolume import correction
        pEqn = fvc.ddt(rho) + psi * correction(
            fvm.ddt(p)) + fvc.div(phi) - fvm.laplacian(rhorUAf, p)

        if corr == nCorr - 1 and nonOrth == nNonOrthCorr:
            pEqn.solve(mesh.solver(word(str(p.name()) + "Final")))
            pass
        else:
            pEqn.solve(mesh.solver(p.name()))
            pass
        if nonOrth == nNonOrthCorr:
            phi.ext_assign(phi + pEqn.flux())
            pass

    # Second part of thermodynamic density update
    thermo.rho().ext_assign(thermo.rho() + psi * p)

    U.ext_assign(U + rUA * fvc.reconstruct((phi - phiU) / rhorUAf))
    U.correctBoundaryConditions()

    DpDt.ext_assign(
        fvc.DDt(surfaceScalarField(word("phiU"), phi / fvc.interpolate(rho)),
                p))

    from Foam.finiteVolume.cfdTools.compressible import rhoEqn
    rhoEqn(rho, phi)

    from Foam.finiteVolume.cfdTools.compressible import compressibleContinuityErrs
    cumulativeContErr = compressibleContinuityErrs(rho, thermo,
                                                   cumulativeContErr)

    # For closed-volume cases adjust the pressure and density levels
    # to obey overall mass continuity
    if closedVolume:
        p.ext_assign(p + (initialMass - fvc.domainIntegrate(psi * p)) /
                     fvc.domainIntegrate(psi))
        thermo.rho().ext_assign(psi * p)
        rho.ext_assign(rho +
                       (initialMass - fvc.domainIntegrate(rho)) / totalVolume)
        pass

    return cumulativeContErr
Example #8
0
def fun_pEqn(mesh, p, rho, psi, p_rgh, U, phi, ghf, gh, DpDt, UEqn, thermo,
             nNonOrthCorr, corr, nCorr, finalIter, cumulativeContErr):

    rho.ext_assign(thermo.rho())

    # Thermodynamic density needs to be updated by psi*d(p) after the
    # pressure solution - done in 2 parts. Part 1:
    thermo.rho().ext_assign(thermo.rho() - psi * p_rgh)

    rUA = 1.0 / UEqn.A()
    from Foam.finiteVolume import surfaceScalarField
    from Foam.OpenFOAM import word
    from Foam import fvc
    rhorUAf = surfaceScalarField(word("(rho*(1|A(U)))"),
                                 fvc.interpolate(rho * rUA))

    U.ext_assign(rUA * UEqn.H())

    phi.ext_assign(
        fvc.interpolate(rho) *
        ((fvc.interpolate(U) & mesh.Sf()) + fvc.ddtPhiCorr(rUA, rho, U, phi)))

    buoyancyPhi = -rhorUAf * ghf * fvc.snGrad(rho) * mesh.magSf()
    phi.ext_assign(phi + buoyancyPhi)

    from Foam import fvm
    from Foam.finiteVolume import correction
    for nonOrth in range(nNonOrthCorr + 1):
        p_rghEqn = fvc.ddt(rho) + psi * correction(
            fvm.ddt(p_rgh)) + fvc.div(phi) - fvm.laplacian(rhorUAf, p_rgh)

        p_rghEqn.solve(
            mesh.solver(
                p_rgh.select((finalIter and corr == nCorr - 1
                              and nonOrth == nNonOrthCorr))))

        if nonOrth == nNonOrthCorr:
            # Calculate the conservative fluxes
            phi.ext_assign(phi + p_rghEqn.flux())

            # Explicitly relax pressure for momentum corrector
            p_rgh.relax()

            # Correct the momentum source with the pressure gradient flux
            # calculated from the relaxed pressure
            U.ext_assign(U + rUA * fvc.reconstruct(
                (buoyancyPhi + p_rghEqn.flux()) / rhorUAf))
            U.correctBoundaryConditions()
            pass

    p.ext_assign(p_rgh + rho * gh)

    # Second part of thermodynamic density update
    thermo.rho().ext_assign(thermo.rho() + psi * p_rgh)

    DpDt.ext_assign(
        fvc.DDt(surfaceScalarField(word("phiU"), phi / fvc.interpolate(rho)),
                p))

    from Foam.finiteVolume.cfdTools.compressible import rhoEqn
    rhoEqn(rho, phi)

    from Foam.finiteVolume.cfdTools.compressible import compressibleContinuityErrs
    cumulativeContErr = compressibleContinuityErrs(rho, thermo,
                                                   cumulativeContErr)

    return cumulativeContErr
Example #9
0
def main_standalone(argc, argv):

    from Foam.OpenFOAM.include import setRootCase
    args = setRootCase(argc, argv)

    from Foam.OpenFOAM.include import createTime
    runTime = createTime(args)

    from Foam.OpenFOAM.include import createMesh
    mesh = createMesh(runTime)

    thermo, p, e, T, psi, mu, U, pbf, rhoBoundaryTypes, rho, rhoU, rhoE, pos, neg, inviscid = _createFields(
        runTime, mesh)

    thermophysicalProperties, Pr = readThermophysicalProperties(runTime, mesh)

    from Foam.finiteVolume.cfdTools.general.include import readTimeControls
    adjustTimeStep, maxCo, maxDeltaT = readTimeControls(runTime)

    fluxScheme = readFluxScheme(mesh)

    from Foam.OpenFOAM import dimensionedScalar, dimVolume, dimTime, word
    v_zero = dimensionedScalar(word("v_zero"), dimVolume / dimTime, 0.0)

    from Foam.OpenFOAM import ext_Info, nl
    ext_Info() << "\nStarting time loop\n" << nl

    while runTime.run():
        # --- upwind interpolation of primitive fields on faces
        from Foam import fvc
        rho_pos = fvc.interpolate(rho, pos, word("reconstruct(rho)"))
        rho_neg = fvc.interpolate(rho, neg, word("reconstruct(rho)"))

        rhoU_pos = fvc.interpolate(rhoU, pos, word("reconstruct(U)"))
        rhoU_neg = fvc.interpolate(rhoU, neg, word("reconstruct(U)"))

        rPsi = 1.0 / psi
        rPsi_pos = fvc.interpolate(rPsi, pos, word("reconstruct(T)"))
        rPsi_neg = fvc.interpolate(rPsi, neg, word("reconstruct(T)"))

        e_pos = fvc.interpolate(e, pos, word("reconstruct(T)"))
        e_neg = fvc.interpolate(e, neg, word("reconstruct(T)"))

        U_pos = rhoU_pos / rho_pos
        U_neg = rhoU_neg / rho_neg

        p_pos = rho_pos * rPsi_pos
        p_neg = rho_neg * rPsi_neg

        phiv_pos = U_pos & mesh.Sf()
        phiv_neg = U_neg & mesh.Sf()

        c = (thermo.Cp() / thermo.Cv() * rPsi).sqrt()
        cSf_pos = fvc.interpolate(c, pos,
                                  word("reconstruct(T)")) * mesh.magSf()
        cSf_neg = fvc.interpolate(c, neg,
                                  word("reconstruct(T)")) * mesh.magSf()

        ap = (phiv_pos + cSf_pos).ext_max(phiv_neg + cSf_neg).ext_max(v_zero)
        am = (phiv_pos - cSf_pos).ext_min(phiv_neg - cSf_neg).ext_min(v_zero)

        a_pos = ap / (ap - am)

        from Foam.finiteVolume import surfaceScalarField
        amaxSf = surfaceScalarField(word("amaxSf"), am.mag().ext_max(ap.mag()))

        aSf = am * a_pos

        if str(fluxScheme) == "Tadmor":
            aSf.ext_assign(-0.5 * amaxSf)
            a_pos.ext_assign(0.5)
            pass

        a_neg = 1.0 - a_pos

        phiv_pos *= a_pos
        phiv_neg *= a_neg

        aphiv_pos = phiv_pos - aSf

        aphiv_neg = phiv_neg + aSf

        # Reuse amaxSf for the maximum positive and negative fluxes
        # estimated by the central scheme
        amaxSf.ext_assign(aphiv_pos.mag().ext_max(aphiv_neg.mag()))

        CoNum, meanCoNum = compressibleCourantNo(mesh, amaxSf, runTime)

        from Foam.finiteVolume.cfdTools.general.include import readTimeControls
        adjustTimeStep, maxCo, maxDeltaT = readTimeControls(runTime)

        from Foam.finiteVolume.cfdTools.general.include import setDeltaT
        runTime = setDeltaT(runTime, adjustTimeStep, maxCo, maxDeltaT, CoNum)

        runTime.increment()

        ext_Info() << "Time = " << runTime.timeName() << nl << nl
        phi = None

        phi = surfaceScalarField(word("phi"),
                                 aphiv_pos * rho_pos + aphiv_neg * rho_neg)

        phiUp = (aphiv_pos * rhoU_pos + aphiv_neg *
                 rhoU_neg) + (a_pos * p_pos + a_neg * p_neg) * mesh.Sf()

        phiEp = aphiv_pos * ( rho_pos * ( e_pos + 0.5*U_pos.magSqr() ) + p_pos ) + aphiv_neg * ( rho_neg * ( e_neg + 0.5 * U_neg.magSqr() ) + p_neg )\
                + aSf * p_pos - aSf * p_neg

        from Foam.finiteVolume import volTensorField
        from Foam import fvc
        tauMC = volTensorField(word("tauMC"), mu * fvc.grad(U).T().dev2())

        # --- Solve density
        from Foam.finiteVolume import solve
        from Foam import fvm
        solve(fvm.ddt(rho) + fvc.div(phi))

        # --- Solve momentum
        solve(fvm.ddt(rhoU) + fvc.div(phiUp))

        U.dimensionedInternalField().ext_assign(
            rhoU.dimensionedInternalField() / rho.dimensionedInternalField())
        U.correctBoundaryConditions()
        rhoU.ext_boundaryField().ext_assign(rho.ext_boundaryField() *
                                            U.ext_boundaryField())

        rhoBydt = rho / runTime.deltaT()

        if not inviscid:
            solve(
                fvm.ddt(rho, U) - fvc.ddt(rho, U) - fvm.laplacian(mu, U) -
                fvc.div(tauMC))
            rhoU.ext_assign(rho * U)
            pass

        # --- Solve energy
        sigmaDotU = (fvc.interpolate(mu) * mesh.magSf() * fvc.snGrad(U) +
                     (mesh.Sf() & fvc.interpolate(tauMC))) & (a_pos * U_pos +
                                                              a_neg * U_neg)

        solve(fvm.ddt(rhoE) + fvc.div(phiEp) - fvc.div(sigmaDotU))

        e.ext_assign(rhoE / rho - 0.5 * U.magSqr())
        e.correctBoundaryConditions()
        thermo.correct()
        from Foam.finiteVolume import volScalarField
        rhoE.ext_boundaryField().ext_assign(
            rho.ext_boundaryField() *
            (e.ext_boundaryField() + 0.5 * U.ext_boundaryField().magSqr()))

        if not inviscid:
            k = volScalarField(word("k"), thermo.Cp() * mu / Pr)

            # The initial C++ expression does not work properly, because of
            #  1. the order of expression arguments computation differs with C++
            #solve( fvm.ddt( rho, e ) - fvc.ddt( rho, e ) - fvm.laplacian( thermo.alpha(), e ) \
            #                                             + fvc.laplacian( thermo.alpha(), e ) - fvc.laplacian( k, T ) )

            solve( -fvc.laplacian( k, T ) + ( fvc.laplacian( thermo.alpha(), e ) \
                                          + (- fvm.laplacian( thermo.alpha(), e ) + (- fvc.ddt( rho, e ) + fvm.ddt( rho, e ) ) ) ) )

            thermo.correct()
            rhoE.ext_assign(rho * (e + 0.5 * U.magSqr()))
            pass

        p.dimensionedInternalField().ext_assign(
            rho.dimensionedInternalField() / psi.dimensionedInternalField())
        p.correctBoundaryConditions()
        rho.ext_boundaryField().ext_assign(psi.ext_boundaryField() *
                                           p.ext_boundaryField())

        runTime.write()

        ext_Info() << "ExecutionTime = " << runTime.elapsedCpuTime() << " s" << \
              "  ClockTime = " << runTime.elapsedClockTime() << " s" << nl << nl

        pass

    ext_Info() << "End\n"

    import os
    return os.EX_OK