Implementation of Temperature Eqn in InterPhaseChangeFoam

Jibran · January 18, 2013, 08:22

Dear All,

Has anyone sucessfully implemented the temperature equation in interphaseChangeFoam?? I followed 'A interphasechangeFoam tutorial by Martin Andersen' but the results seem to be quite inaccurate. I have attached the relevant files below.

ALPHA1

Code:

 
FoamFile
{
    version     2.0;
    format      ascii;
    class       volScalarField;
    location    "0";
    object      alpha;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
dimensions      [0 0 0 0 0 0 0];
internalField   uniform 0;
boundaryField
{
    axis
    {
        type            symmetryPlane;
    }
    
    right_wall
    {
        type            constantAlphaContactAngle;
        theta0          10;
        limit  gradient;
        value           uniform 0;
    }
    
    lower_wall
    {
        type            zeroGradient;
    }
    
    atmosphere
    {
        type  zeroGradient;    
    }
    
    default_faces
    {
        type            empty;
    }
}

P_RGH

Code:

 
FoamFile
{
    version     2.0;
    format      ascii;
    class       volScalarField;
    location    "0";
    object      p_rgh;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
dimensions      [1 -1 -2 0 0];
internalField   uniform 100000;
boundaryField
{
    axis
    {
        type            symmetryPlane;
    }
    
    right_wall
    {
        type            fixedFluxPressure;
        adjoint         no;
    }
    
    lower_wall
    {
        type            buoyantPressure;
    }
    
    atmosphere
    { 
        type            fixedValue;
        value           uniform 100000;
    }
    
    default_faces
    {
        type            empty;
    }
}

T

Code:

 
FoamFile
{
    version     2.0;
    format      ascii;
    class       volScalarField;
    location    "0";
    object      T;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
dimensions      [0 0 0 1 0]; // [K]
internalField   uniform 280.15;
boundaryField
{
    axis
    {
        type            symmetryPlane;
    }
    
    right_wall
    {
        type            fixedValue;
        value         uniform 300.15;
    }
    
    lower_wall
    {
        type            fixedValue;
        value         uniform 300.15;
    }
    
    atmosphere
    {
        type            fixedValue;   
        value         uniform 280.15;
    }
    default_faces
    {
        type            empty;
    }
}

U

Code:

 
FoamFile
{
    version     2.0;
    format      ascii;
    class       volVectorField;
    location    "0";
    object      U;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
dimensions      [0 1 -1 0 0];
internalField   uniform (0 0 0);
boundaryField
{
    axis
    {
        type            symmetryPlane;
    }
    right_wall
    {
        type            fixedValue;
        value           uniform (0 0 0);
    }
    lower_wall
    {
        type            fixedValue;
        value           uniform (0 0 0);
    }
    atmosphere
    {
        type            fixedValue;        
        value           uniform (0 0 0);
    }
    
    default_faces
    {
        type            empty;
    }
}

TRANSPORT PROPERTIES

Code:

FoamFile
{
    version     2.0;
    format      ascii;
    class       dictionary;
    object      transportProperties;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
phaseChange on;
 
phaseChangeTwoPhaseMixture Kunz;
 
sigma           sigma  [1 0 -2 0 0 0 0] 0.07;
 
DT   DT  [0 2 -1 0 0 0 0] 0.02; // [m^2/s]
 
phase1
{
    transportModel Newtonian;
    nu              nu [0 2 -1 0 0 0 0] 5.5e-07;
    rho             rho [1 -3 0 0 0 0 0] 988;
}
 
phase2
{
    transportModel Newtonian;
    nu              nu [0 2 -1 0 0 0 0] 4.273e-04;
    rho             rho [1 -3 0 0 0 0 0] 0.02308;
}
KunzCoeffs
{
    UInf            UInf   [0 1 -1 0 0 0 0]     5.0;
    tInf            tInf   [0 0 1 0 0 0 0]       0.016; // L = 0.08 m
    Cc              Cc     [0 0 0 0 0 0 0]      100;
    Cv              Cv     [0 0 0 0 0 0 0]      100;
}
MerkleCoeffs
{ 
    UInf            UInf   [0 1 -1 0 0 0 0]     5.0;
    tInf            tInf   [0 0 1 0 0 0 0]       0.016;  // L = 0.08 m
    Cc              Cc     [0 0 0 0 0 0 0]      1;
    Cv              Cv     [0 0 0 0 0 0 0]      1;
}
SchnerrSauerCoeffs
{
    n                n      [0 -3 0 0 0 0 0]     1.6e+13;
    dNuc           dNuc  [0 1 0 0 0 0 0]     2.0e-06;
    Cc              Cc     [0 0 0 0 0 0 0]      1;
    Cv              Cv     [0 0 0 0 0 0 0]      1;
}

In my results the temperature is going to a maximum of 370K when a value of 300.15K is specified on the right and bottom walls. Any idea where the error is???

abe · April 8, 2013, 08:38

Which version of openfoam do you use?
Have you been able to get good results from new versions of OF (i.e. 2.1 or 2.2)?

ABE

Jibran · April 10, 2013, 06:52

I am using 2.1 however compressibleInterFoam of 2.2 might be a good starting point as it solves for energy equation.

abe · April 10, 2013, 06:56

Hi Jibran,

do you simulate cavitation?

Jibran · April 10, 2013, 07:36

Hi. I am working on interfacial evaporation and condensation. Are you doing something similar?

abe · April 10, 2013, 08:37

I think, the method used in interPhasechange solver is a relatively different. In this case evaporation or condensation can occur anywhere which has pressure lower than saturation pressure. While in the interfacial method, phase change just occur in the interface of the two phases (am I right?)

Jibran · April 10, 2013, 10:17

Yes that is correct. Therefore I am using a modified phase change model. By including terms such as "alpha1*(1-alpha1)" in the phase change equations one can ensure that the evaporation and condensation takes place just at the interface.

abe · April 10, 2013, 10:26

Do you have get any results?
are the both phases considered compressible or just the vapor phase?

Jibran · April 15, 2013, 06:29

I have some results which seem to be reasonable.
However, I need to validate them.
Yes both phases are compressible.

mecman · September 19, 2013, 01:48

Quote:

Originally Posted by Jibran

Dear All,

Has anyone sucessfully implemented the temperature equation in interphaseChangeFoam?? I followed 'A interphasechangeFoam tutorial by Martin Andersen' but the results seem to be quite inaccurate. I have attached the relevant files below.

ALPHA1

Code:

 
FoamFile
{
    version     2.0;
    format      ascii;
    class       volScalarField;
    location    "0";
    object      alpha;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
dimensions      [0 0 0 0 0 0 0];
internalField   uniform 0;
boundaryField
{
    axis
    {
        type            symmetryPlane;
    }
    
    right_wall
    {
        type            constantAlphaContactAngle;
        theta0          10;
        limit  gradient;
        value           uniform 0;
    }
    
    lower_wall
    {
        type            zeroGradient;
    }
    
    atmosphere
    {
        type  zeroGradient;    
    }
    
    default_faces
    {
        type            empty;
    }
}

P_RGH

Code:

 
FoamFile
{
    version     2.0;
    format      ascii;
    class       volScalarField;
    location    "0";
    object      p_rgh;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
dimensions      [1 -1 -2 0 0];
internalField   uniform 100000;
boundaryField
{
    axis
    {
        type            symmetryPlane;
    }
    
    right_wall
    {
        type            fixedFluxPressure;
        adjoint         no;
    }
    
    lower_wall
    {
        type            buoyantPressure;
    }
    
    atmosphere
    { 
        type            fixedValue;
        value           uniform 100000;
    }
    
    default_faces
    {
        type            empty;
    }
}

T

Code:

 
FoamFile
{
    version     2.0;
    format      ascii;
    class       volScalarField;
    location    "0";
    object      T;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
dimensions      [0 0 0 1 0]; // [K]
internalField   uniform 280.15;
boundaryField
{
    axis
    {
        type            symmetryPlane;
    }
    
    right_wall
    {
        type            fixedValue;
        value         uniform 300.15;
    }
    
    lower_wall
    {
        type            fixedValue;
        value         uniform 300.15;
    }
    
    atmosphere
    {
        type            fixedValue;   
        value         uniform 280.15;
    }
    default_faces
    {
        type            empty;
    }
}

U

Code:

 
FoamFile
{
    version     2.0;
    format      ascii;
    class       volVectorField;
    location    "0";
    object      U;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
dimensions      [0 1 -1 0 0];
internalField   uniform (0 0 0);
boundaryField
{
    axis
    {
        type            symmetryPlane;
    }
    right_wall
    {
        type            fixedValue;
        value           uniform (0 0 0);
    }
    lower_wall
    {
        type            fixedValue;
        value           uniform (0 0 0);
    }
    atmosphere
    {
        type            fixedValue;        
        value           uniform (0 0 0);
    }
    
    default_faces
    {
        type            empty;
    }
}

TRANSPORT PROPERTIES

Code:

FoamFile
{
    version     2.0;
    format      ascii;
    class       dictionary;
    object      transportProperties;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
phaseChange on;
 
phaseChangeTwoPhaseMixture Kunz;
 
sigma           sigma  [1 0 -2 0 0 0 0] 0.07;
 
DT   DT  [0 2 -1 0 0 0 0] 0.02; // [m^2/s]
 
phase1
{
    transportModel Newtonian;
    nu              nu [0 2 -1 0 0 0 0] 5.5e-07;
    rho             rho [1 -3 0 0 0 0 0] 988;
}
 
phase2
{
    transportModel Newtonian;
    nu              nu [0 2 -1 0 0 0 0] 4.273e-04;
    rho             rho [1 -3 0 0 0 0 0] 0.02308;
}
KunzCoeffs
{
    UInf            UInf   [0 1 -1 0 0 0 0]     5.0;
    tInf            tInf   [0 0 1 0 0 0 0]       0.016; // L = 0.08 m
    Cc              Cc     [0 0 0 0 0 0 0]      100;
    Cv              Cv     [0 0 0 0 0 0 0]      100;
}
MerkleCoeffs
{ 
    UInf            UInf   [0 1 -1 0 0 0 0]     5.0;
    tInf            tInf   [0 0 1 0 0 0 0]       0.016;  // L = 0.08 m
    Cc              Cc     [0 0 0 0 0 0 0]      1;
    Cv              Cv     [0 0 0 0 0 0 0]      1;
}
SchnerrSauerCoeffs
{
    n                n      [0 -3 0 0 0 0 0]     1.6e+13;
    dNuc           dNuc  [0 1 0 0 0 0 0]     2.0e-06;
    Cc              Cc     [0 0 0 0 0 0 0]      1;
    Cv              Cv     [0 0 0 0 0 0 0]      1;
}

In my results the temperature is going to a maximum of 370K when a value of 300.15K is specified on the right and bottom walls. Any idea where the error is???

Hi Jibran and abe
Do you modified youre solver (interPhasechangrFoam) by adding T.eqn and source term?i want simulate evaporation and condensation and i use interPhasechangeFoam solver.i implemented the temperature equation( A interphasechangeFoam tutorial by Martin Andersen) but i dnt know how modified the solver by source term and T.eqn for phase change with increasing Temperature.

Kanarya · June 2, 2015, 08:52

Hi All,

I am trying to simulate condensation with interPhaseChangeFoam by adding scalar T. But it gives me the following error:

PHP Code:


			
time step continuity errors : sum local = 1.15855e-05, global = -1.19144e-16, cumulative = -1.19144e-16

GAMG:  Solving for pcorr, Initial residual = 1, Final residual = 3.48266e+19, No Iterations 50

GAMG:  Solving for pcorr, Initial residual = 0.965555, Final residual = 1.08509e+21, No Iterations 50

time step continuity errors : sum local = 4.51124e+35, global = -1.41141e+28, cumulative = -1.41141e+28

Courant Number mean: 3.09991e+35 max: 5.41686e+38



Starting time loop



Courant Number mean: 0.00057227 max: 1

deltaT = 1.84609e-47

Time = 1.84609e-47



#0  Foam::error::printStack(Foam::Ostream&) in "/usr/local/OpenFOAM/OpenFOAM-2.1.0/platforms/linux64GccDPOpt/lib/libOpenFOAM.so"

#1  Foam::sigFpe::sigHandler(int) in "/usr/local/OpenFOAM/OpenFOAM-2.1.0/platforms/linux64GccDPOpt/lib/libOpenFOAM.so"

#2  

 at sigaction.c:0

#3  

 in "/home/links/rek209/OpenFOAM/rek209-2.1.0/platforms/linux64GccDPOpt/bin/myInterPhaseChangeFoam"

#4  

 in "/home/links/rek209/OpenFOAM/rek209-2.1.0/platforms/linux64GccDPOpt/bin/myInterPhaseChangeFoam"

#5  

 in "/home/links/rek209/OpenFOAM/rek209-2.1.0/platforms/linux64GccDPOpt/bin/myInterPhaseChangeFoam"

#6  __libc_start_main in "/lib64/libc.so.6"

#7  

 in "/home/links/rek209/OpenFOAM/rek209-2.1.0/platforms/linux64GccDPOpt/bin/myInterPhaseChangeFoam"

Floating point exception

I am using following BC:
for p_rhg:

PHP Code:


			
/*--------------------------------*- C++ -*----------------------------------*\

| =========                 |                                                 |

| \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox           |

|  \\    /   O peration     | Version:  2.3.1                                 |

|   \\  /    A nd           | Web:      www.OpenFOAM.org                      |

|    \\/     M anipulation  |                                                 |

\*---------------------------------------------------------------------------*/

FoamFile

{

    version     2.0;

    format      ascii;

    class       volScalarField;

    location    "0";

    object      p_rgh;

}

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



dimensions      [1 -1 -2 0 0 0 0];



internalField   uniform 1e5;



boundaryField

{

    inlet

    

        {

         type            zeroGradient;

    }

    



   outlet

    {

        type            fixedValue;

        value           $internalField;

    }



    

  hot_wall

    {

         type           fixedFluxPressure;

adjoint no;

    }

    ocold_wall

   {

         type           fixedFluxPressure;

adjoint no;

    }

    icold_wall

    { 

        type           fixedFluxPressure;

adjoint no;

    }



}



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

for alpha1:

PHP Code:


			
/*--------------------------------*- C++ -*----------------------------------*\

| =========                 |                                                 |

| \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox           |

|  \\    /   O peration     | Version:  2.1.0                                 |

|   \\  /    A nd           | Web:      www.OpenFOAM.org                      |

|    \\/     M anipulation  |                                                 |

\*---------------------------------------------------------------------------*/

FoamFile

{

    version     2.0;

    format      ascii;

    class       volScalarField;

    location    "0";

    object      alpha1;

}

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



dimensions      [0 0 0 0 0];



internalField   uniform 0.00001;



boundaryField

{

    inlet

    {

         type            fixedValue;

        value           $internalField;

    }



    outlet

    {

        type            inletOutlet;

        inletValue      $internalField;

    }



    

    hot_wall

    {

        type            zeroGradient;

    }

    icold_wall

    {

        type            zeroGradient;

    }

    ocold_wall

    {

        type            zeroGradient;

    }



}



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

and for U

PHP Code:


			
/*--------------------------------*- C++ -*----------------------------------*\

| =========                 |                                                 |

| \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox           |

|  \\    /   O peration     | Version:  2.3.1                                 |

|   \\  /    A nd           | Web:      www.OpenFOAM.org                      |

|    \\/     M anipulation  |                                                 |

\*---------------------------------------------------------------------------*/

FoamFile

{

    version     2.0;

    format      ascii;

    class       volVectorField;

    object      U;

}

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



dimensions      [0 1 -1 0 0 0 0];



internalField   uniform (0 0 5.199);



boundaryField

{

    inlet

    {

        type            fixedValue;

        value           $internalField;

    }



    outlet

{

        type            pressureInletOutletVelocity;

        phi             phi;

        value           $internalField;

}

    hot_wall

    {

        type            fixedValue;

        value           uniform (0 0 0);

    }



 ocold_wall

    {

        type            fixedValue;

        value           uniform (0 0 0);

    }

icold_wall

    {

        type            fixedValue;

        value           uniform (0 0 0);

    }



}



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

and fr T

PHP Code:


			
/*--------------------------------*- C++ -*----------------------------------*\

| =========                 |                                                 |

| \\      /  F ield         | OpenFOAM: The Open Source CFD Toolbox           |

|  \\    /   O peration     | Version:  2.3.1                                 |

|   \\  /    A nd           | Web:      www.OpenFOAM.org                      |

|    \\/     M anipulation  |                                                 |

\*---------------------------------------------------------------------------*/

FoamFile

{

    version     2.0;

    format      ascii;

    class       volScalarField;

    object      T;

}

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



dimensions      [0 0 0 1 0 0 0];



internalField   uniform 366.85;



boundaryField

{

    hot_wall

    {

         type            fixedValue;

        value           uniform 293.15;

    }

   ocold_wall

    {

         type            zeroGradient;

        

    }

icold_wall

    {

         type            zeroGradient;



    }



    inlet

    {

        type            fixedValue;

        value           uniform 366.85;

    }

    outlet

    {

        type            zeroGradient;

    }

}



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

I am using version 2.1.0 for it...
can you hep me to fix the problem?

thanks!

Kanarya · June 2, 2015, 10:33

Hi Jibran,

Did you add this term (alpha1*(1-alpha1)) to alphaEqn.H?
Did you get the results?

Thanks

Quote:

Originally Posted by Jibran

Yes that is correct. Therefore I am using a modified phase change model. By including terms such as "alpha1*(1-alpha1)" in the phase change equations one can ensure that the evaporation and condensation takes place just at the interface.

gaza · June 17, 2015, 06:10

Hi Kanaraya
It would be better to use OF2.3.
You can try to decrease Courant number. If you use model from Andersen tutorial it give you wrong results. I try to do use his model for condensation on vertical wall and solver always crashed. It is due to bad model for mass flux.

Kanarya · June 17, 2015, 06:19

Hi Gaza,
thanks for your reply!
Did you manage to get another model?
Or how did you solve your problem?

thanks!

Quote:

Originally Posted by gaza

Hi Kanaraya
It would be better to use OF2.3.
You can try to decrease Courant number. If you use model from Andersen tutorial it give you wrong results. I try to do use his model for condensation on vertical wall and solver always crashed. It is due to bad model for mass flux.

gaza · June 17, 2015, 11:47

Hi Kanarya,
I did not solve my problem. I only know that interPhaseChangeFoam is good for cavitation mass transfer models. For heat transfer one has to change the main code a bit and write own functions
for mDotAlphal and mDotP.
Solver is constructed in that way that in alpha equation (alphaEqn.H) condensation mass flux is multiplied by (1 - alpha) and evaporation mass flux is multiplied by alpha. So you have to: 1) adjust your implementation for mass fluxes to the solver or 2) implement them as they should be and change the solver (alpha eqn. and lines in MULES where vDot variables are used).
The same is true about mDotP function.

I think that it would be better to implement model based on TSat not for pSat.

June 17, 2015, 06:10		#13
gaza Senior Member Przemek Join Date: Jun 2011 Posts: 249 Rep Power: 16	Hi Kanaraya It would be better to use OF2.3. You can try to decrease Courant number. If you use model from Andersen tutorial it give you wrong results. I try to do use his model for condensation on vertical wall and solver always crashed. It is due to bad model for mass flux. __________________ best regards pblasiak

June 17, 2015, 11:47		#15
gaza Senior Member Przemek Join Date: Jun 2011 Posts: 249 Rep Power: 16	Hi Kanarya, I did not solve my problem. I only know that interPhaseChangeFoam is good for cavitation mass transfer models. For heat transfer one has to change the main code a bit and write own functions for mDotAlphal and mDotP. Solver is constructed in that way that in alpha equation (alphaEqn.H) condensation mass flux is multiplied by (1 - alpha) and evaporation mass flux is multiplied by alpha. So you have to: 1) adjust your implementation for mass fluxes to the solver or 2) implement them as they should be and change the solver (alpha eqn. and lines in MULES where vDot variables are used). The same is true about mDotP function. I think that it would be better to implement model based on TSat not for pSat. __________________ best regards pblasiak

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UDFs for Scalar Eqn - Fluid/Solid HT	Greg Perkins	FLUENT	0	October 14, 2000 00:03
UDFs for Scalar Eqn - Fluid/Solid HT	Greg Perkins	FLUENT	0	October 11, 2000 04:43

April 8, 2013, 08:38		#2
abe Member ABE Join Date: Jul 2012 Posts: 46 Rep Power: 14	Which version of openfoam do you use? Have you been able to get good results from new versions of OF (i.e. 2.1 or 2.2)? ABE

April 10, 2013, 06:52		#3
Jibran Member Jibran Join Date: Oct 2012 Location: UK Posts: 61 Blog Entries: 1 Rep Power: 15	I am using 2.1 however compressibleInterFoam of 2.2 might be a good starting point as it solves for energy equation.

April 10, 2013, 06:56		#4
abe Member ABE Join Date: Jul 2012 Posts: 46 Rep Power: 14	Hi Jibran, do you simulate cavitation?

April 10, 2013, 07:36		#5
Jibran Member Jibran Join Date: Oct 2012 Location: UK Posts: 61 Blog Entries: 1 Rep Power: 15	Hi. I am working on interfacial evaporation and condensation. Are you doing something similar?

April 10, 2013, 08:37		#6
abe Member ABE Join Date: Jul 2012 Posts: 46 Rep Power: 14	I think, the method used in interPhasechange solver is a relatively different. In this case evaporation or condensation can occur anywhere which has pressure lower than saturation pressure. While in the interfacial method, phase change just occur in the interface of the two phases (am I right?)

April 10, 2013, 10:17		#7
Jibran Member Jibran Join Date: Oct 2012 Location: UK Posts: 61 Blog Entries: 1 Rep Power: 15	Yes that is correct. Therefore I am using a modified phase change model. By including terms such as "alpha1*(1-alpha1)" in the phase change equations one can ensure that the evaporation and condensation takes place just at the interface.

April 10, 2013, 10:26		#8
abe Member ABE Join Date: Jul 2012 Posts: 46 Rep Power: 14	Do you have get any results? are the both phases considered compressible or just the vapor phase?

April 15, 2013, 06:29		#9
Jibran Member Jibran Join Date: Oct 2012 Location: UK Posts: 61 Blog Entries: 1 Rep Power: 15	I have some results which seem to be reasonable. However, I need to validate them. Yes both phases are compressible.

June 2, 2015, 08:52		#11
Kanarya Senior Member Join Date: May 2011 Posts: 231 Rep Power: 16	Hi All, I am trying to simulate condensation with interPhaseChangeFoam by adding scalar T. But it gives me the following error: PHP Code: time step continuity errors : sum local = 1.15855e-05, global = -1.19144e-16, cumulative = -1.19144e-16 GAMG: Solving for pcorr, Initial residual = 1, Final residual = 3.48266e+19, No Iterations 50 GAMG: Solving for pcorr, Initial residual = 0.965555, Final residual = 1.08509e+21, No Iterations 50 time step continuity errors : sum local = 4.51124e+35, global = -1.41141e+28, cumulative = -1.41141e+28 Courant Number mean: 3.09991e+35 max: 5.41686e+38 Starting time loop Courant Number mean: 0.00057227 max: 1 deltaT = 1.84609e-47 Time = 1.84609e-47 #0 Foam::error::printStack(Foam::Ostream&) in "/usr/local/OpenFOAM/OpenFOAM-2.1.0/platforms/linux64GccDPOpt/lib/libOpenFOAM.so" #1 Foam::sigFpe::sigHandler(int) in "/usr/local/OpenFOAM/OpenFOAM-2.1.0/platforms/linux64GccDPOpt/lib/libOpenFOAM.so" #2 at sigaction.c:0 #3 in "/home/links/rek209/OpenFOAM/rek209-2.1.0/platforms/linux64GccDPOpt/bin/myInterPhaseChangeFoam" #4 in "/home/links/rek209/OpenFOAM/rek209-2.1.0/platforms/linux64GccDPOpt/bin/myInterPhaseChangeFoam" #5 in "/home/links/rek209/OpenFOAM/rek209-2.1.0/platforms/linux64GccDPOpt/bin/myInterPhaseChangeFoam" #6 __libc_start_main in "/lib64/libc.so.6" #7 in "/home/links/rek209/OpenFOAM/rek209-2.1.0/platforms/linux64GccDPOpt/bin/myInterPhaseChangeFoam" Floating point exception I am using following BC: for p_rhg: PHP Code: /--------------------------------- C++ -----------------------------------\ \| ========= \| \| \| \\ / F ield \| OpenFOAM: The Open Source CFD Toolbox \| \| \\ / O peration \| Version: 2.3.1 \| \| \\ / A nd \| Web: www.OpenFOAM.org \| \| \\/ M anipulation \| \| \---------------------------------------------------------------------------/ FoamFile { version 2.0; format ascii; class volScalarField; location "0"; object p_rgh; } // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // dimensions [1 -1 -2 0 0 0 0]; internalField uniform 1e5; boundaryField { inlet { type zeroGradient; } outlet { type fixedValue; value $internalField; } hot_wall { type fixedFluxPressure; adjoint no; } ocold_wall { type fixedFluxPressure; adjoint no; } icold_wall { type fixedFluxPressure; adjoint no; } } // ************************************************************************* // for alpha1: PHP Code: /--------------------------------- C++ -----------------------------------\ \| ========= \| \| \| \\ / F ield \| OpenFOAM: The Open Source CFD Toolbox \| \| \\ / O peration \| Version: 2.1.0 \| \| \\ / A nd \| Web: www.OpenFOAM.org \| \| \\/ M anipulation \| \| \---------------------------------------------------------------------------/ FoamFile { version 2.0; format ascii; class volScalarField; location "0"; object alpha1; } // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // dimensions [0 0 0 0 0]; internalField uniform 0.00001; boundaryField { inlet { type fixedValue; value $internalField; } outlet { type inletOutlet; inletValue $internalField; } hot_wall { type zeroGradient; } icold_wall { type zeroGradient; } ocold_wall { type zeroGradient; } } // ************************************************************************* // and for U PHP Code: /--------------------------------- C++ -----------------------------------\ \| ========= \| \| \| \\ / F ield \| OpenFOAM: The Open Source CFD Toolbox \| \| \\ / O peration \| Version: 2.3.1 \| \| \\ / A nd \| Web: www.OpenFOAM.org \| \| \\/ M anipulation \| \| \---------------------------------------------------------------------------/ FoamFile { version 2.0; format ascii; class volVectorField; object U; } // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // dimensions [0 1 -1 0 0 0 0]; internalField uniform (0 0 5.199); boundaryField { inlet { type fixedValue; value $internalField; } outlet { type pressureInletOutletVelocity; phi phi; value $internalField; } hot_wall { type fixedValue; value uniform (0 0 0); } ocold_wall { type fixedValue; value uniform (0 0 0); } icold_wall { type fixedValue; value uniform (0 0 0); } } // ************************************************************************* // and fr T PHP Code: /--------------------------------- C++ -----------------------------------\ \| ========= \| \| \| \\ / F ield \| OpenFOAM: The Open Source CFD Toolbox \| \| \\ / O peration \| Version: 2.3.1 \| \| \\ / A nd \| Web: www.OpenFOAM.org \| \| \\/ M anipulation \| \| \---------------------------------------------------------------------------/ FoamFile { version 2.0; format ascii; class volScalarField; object T; } // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // dimensions [0 0 0 1 0 0 0]; internalField uniform 366.85; boundaryField { hot_wall { type fixedValue; value uniform 293.15; } ocold_wall { type zeroGradient; } icold_wall { type zeroGradient; } inlet { type fixedValue; value uniform 366.85; } outlet { type zeroGradient; } } // ************************************************************************* // I am using version 2.1.0 for it... can you hep me to fix the problem? thanks!