CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > OpenFOAM > OpenFOAM Running, Solving & CFD

reactingFoam running error

Register Blogs Members List Search Today's Posts Mark Forums Read

Like Tree1Likes
  • 1 Post By ghazal_1989

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   January 17, 2017, 10:49
Default reactingFoam running error
  #1
New Member
 
Zhenlan GAO
Join Date: Oct 2015
Location: France
Posts: 17
Rep Power: 7
tubois is on a distinguished road
I tried to set up the Tutorial Eleven reacting foam found http://www.cfd.at/downloads/2014_OFoam_Tut_Complete.pdf

I got the error as below. Can someone help me?

/*---------------------------------------------------------------------------*\
| ========= | |
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
| \\ / O peration | Version: v1612+ |
| \\ / A nd | Web: www.OpenFOAM.com |
| \\/ M anipulation | |
\*---------------------------------------------------------------------------*/
Build : v1612+
Exec : reactingFoam
Date : Jan 17 2017
Time : 16:47:09
Host : "belledonne"
PID : 6002
Case : /home/gao/OpenFOAM/gao-v1612+/run/counterFlowFlame2D_v2
nProcs : 1
sigFpe : Enabling floating point exception trapping (FOAM_SIGFPE).
fileModificationChecking : Monitoring run-time modified files using timeStampMaster (fileModificationSkew 10)
allowSystemOperations : Allowing user-supplied system call operations

// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
Create time

Create mesh for time = 0


PIMPLE: Operating solver in PISO mode

Creating reaction model

Selecting combustion model laminar<psiChemistryCombustion>
Selecting chemistry type
{
chemistrySolver EulerImplicit;
chemistryThermo psi;
}

Selecting thermodynamics package
{
type hePsiThermo;
mixture reactingMixture;
transport sutherland;
thermo janaf;
energy sensibleEnthalpy;
equationOfState perfectGas;
specie specie;
}

Selecting chemistryReader foamChemistryReader
elements not defined in "/home/gao/OpenFOAM/gao-v1612+/run/counterFlowFlame2D_v2/constant/reactions"
chemistryModel: Number of species = 5 and reactions = 1
using integrated reaction rate
Reading field U

Reading/calculating face flux field phi

Creating turbulence model.

Selecting turbulence model type laminar
Selecting laminar stress model Stokes
Creating field dpdt

Creating field kinetic energy K

No MRF models present

No finite volume options present

Courant Number mean: 2.99581e-08 max: 1.72209e-05

Starting time loop

Courant Number mean: 2.99581e-08 max: 1.72209e-05
deltaT = 1.2e-06
Time = 1.2e-06

diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
PIMPLE: iteration 1
#0 Foam::error:rintStack(Foam::Ostream&) at ??:?
#1 Foam::sigFpe::sigHandler(int) at ??:?
#2 ? in "/lib/x86_64-linux-gnu/libc.so.6"
#3 Foam::divide(Foam::Field<double>&, Foam::UList<double> const&, Foam::UList<double> const&) at ??:?
#4 Foam::tmp<Foam::GeometricField<double, Foam::fvPatchField, Foam::volMesh> > Foam:perator/<Foam::fvPatchField, Foam::volMesh>(Foam::tmp<Foam::GeometricField<doub le, Foam::fvPatchField, Foam::volMesh> > const&, Foam::tmp<Foam::GeometricField<double, Foam::fvPatchField, Foam::volMesh> > const&) at ??:?
#5 Foam::fluidThermo::nu() const at ??:?
#6 Foam::laminarModels::Stokes<Foam::ThermalDiffusivi ty<Foam::CompressibleTurbulenceModel<Foam::fluidTh ermo> > >::nuEff() const at ??:?
#7 Foam::linearViscousStress<Foam::laminarModel<Foam: :ThermalDiffusivity<Foam::CompressibleTurbulenceMo del<Foam::fluidThermo> > > >::divDevRhoReff(Foam::GeometricField<Foam::Vector <double>, Foam::fvPatchField, Foam::volMesh>&) const at ??:?
#8 ? at ??:?
#9 __libc_start_main in "/lib/x86_64-linux-gnu/libc.so.6"
#10 ? at ??:?
Exception en point flottant (core dumped)
Attached Files
File Type: gz counterFlowFlame2D_v2.tar.gz (54.1 KB, 8 views)
tubois is offline   Reply With Quote

Old   January 18, 2017, 05:27
Default
  #2
New Member
 
Zhenlan GAO
Join Date: Oct 2015
Location: France
Posts: 17
Rep Power: 7
tubois is on a distinguished road
The tutorial is prepared with OF 2.3.0
So I run this case with my old version OF 2.4.0 with three small adaptions, the case starts running.

So I am wondering when did OF introduce some bugs here?

Can someone help me to fix the bug? I am new to OF.


Quote:
Originally Posted by tubois View Post
I tried to set up the Tutorial Eleven reacting foam found http://www.cfd.at/downloads/2014_OFoam_Tut_Complete.pdf

I got the error as below. Can someone help me?

/*---------------------------------------------------------------------------*\
| ========= | |
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
| \\ / O peration | Version: v1612+ |
| \\ / A nd | Web: www.OpenFOAM.com |
| \\/ M anipulation | |
\*---------------------------------------------------------------------------*/
Build : v1612+
Exec : reactingFoam
Date : Jan 17 2017
Time : 16:47:09
Host : "belledonne"
PID : 6002
Case : /home/gao/OpenFOAM/gao-v1612+/run/counterFlowFlame2D_v2
nProcs : 1
sigFpe : Enabling floating point exception trapping (FOAM_SIGFPE).
fileModificationChecking : Monitoring run-time modified files using timeStampMaster (fileModificationSkew 10)
allowSystemOperations : Allowing user-supplied system call operations

// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
Create time

Create mesh for time = 0


PIMPLE: Operating solver in PISO mode

Creating reaction model

Selecting combustion model laminar<psiChemistryCombustion>
Selecting chemistry type
{
chemistrySolver EulerImplicit;
chemistryThermo psi;
}

Selecting thermodynamics package
{
type hePsiThermo;
mixture reactingMixture;
transport sutherland;
thermo janaf;
energy sensibleEnthalpy;
equationOfState perfectGas;
specie specie;
}

Selecting chemistryReader foamChemistryReader
elements not defined in "/home/gao/OpenFOAM/gao-v1612+/run/counterFlowFlame2D_v2/constant/reactions"
chemistryModel: Number of species = 5 and reactions = 1
using integrated reaction rate
Reading field U

Reading/calculating face flux field phi

Creating turbulence model.

Selecting turbulence model type laminar
Selecting laminar stress model Stokes
Creating field dpdt

Creating field kinetic energy K

No MRF models present

No finite volume options present

Courant Number mean: 2.99581e-08 max: 1.72209e-05

Starting time loop

Courant Number mean: 2.99581e-08 max: 1.72209e-05
deltaT = 1.2e-06
Time = 1.2e-06

diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
PIMPLE: iteration 1
#0 Foam::error:rintStack(Foam::Ostream&) at ??:?
#1 Foam::sigFpe::sigHandler(int) at ??:?
#2 ? in "/lib/x86_64-linux-gnu/libc.so.6"
#3 Foam::divide(Foam::Field<double>&, Foam::UList<double> const&, Foam::UList<double> const&) at ??:?
#4 Foam::tmp<Foam::GeometricField<double, Foam::fvPatchField, Foam::volMesh> > Foam:perator/<Foam::fvPatchField, Foam::volMesh>(Foam::tmp<Foam::GeometricField<doub le, Foam::fvPatchField, Foam::volMesh> > const&, Foam::tmp<Foam::GeometricField<double, Foam::fvPatchField, Foam::volMesh> > const&) at ??:?
#5 Foam::fluidThermo::nu() const at ??:?
#6 Foam::laminarModels::Stokes<Foam::ThermalDiffusivi ty<Foam::CompressibleTurbulenceModel<Foam::fluidTh ermo> > >::nuEff() const at ??:?
#7 Foam::linearViscousStress<Foam::laminarModel<Foam: :ThermalDiffusivity<Foam::CompressibleTurbulenceMo del<Foam::fluidThermo> > > >::divDevRhoReff(Foam::GeometricField<Foam::Vector <double>, Foam::fvPatchField, Foam::volMesh>&) const at ??:?
#8 ? at ??:?
#9 __libc_start_main in "/lib/x86_64-linux-gnu/libc.so.6"
#10 ? at ??:?
Exception en point flottant (core dumped)
tubois is offline   Reply With Quote

Old   February 21, 2017, 09:20
Default reactingFoam solver errors
  #3
New Member
 
Join Date: Jan 2017
Posts: 12
Rep Power: 6
ghazal_1989 is on a distinguished road
Hi all,

As a openFoam beginner, I've run a simulation in reactingFoam and unfortunately I just got these codes with No iteration ! Is there anyone who would help me please?


.
.
.

Time = 2.46472e-05

diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
PIMPLE: iteration 1
DILUPBiCG: Solving for O2, Initial residual = 0, Final residual = 0, No Iterations 0
DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0
DILUPBiCG: Solving for CH4, Initial residual = 0, Final residual = 0, No Iterations 0
DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0
DILUPBiCG: Solving for h, Initial residual = 7.83352e-07, Final residual = 7.83352e-07, No Iterations 0
min/max(T) = 358.241, 1499.98
DICPCG: Solving for p, Initial residual = 5.76649e-07, Final residual = 5.76649e-07, No Iterations 0
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
time step continuity errors : sum local = 7.65015e-07, global = -2.09684e-17, cumulative = -0.00201457
rho max/min : 2.50857 2.33323e-06
DICPCG: Solving for p, Initial residual = 5.76649e-07, Final residual = 5.76649e-07, No Iterations 0
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
time step continuity errors : sum local = 7.65015e-07, global = -2.08342e-17, cumulative = -0.00201457
rho max/min : 2.50857 2.33323e-06
ExecutionTime = 118.72 s ClockTime = 120 s

Courant Number mean: 6.95254e-05 max: 0.399999
deltaT = 9.51118e-12
Time = 2.46472e-05

diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
PIMPLE: iteration 1
DILUPBiCG: Solving for O2, Initial residual = 0, Final residual = 0, No Iterations 0
DILUPBiCG: Solving for H2O, Initial residual = 0, Final residual = 0, No Iterations 0
DILUPBiCG: Solving for CH4, Initial residual = 0, Final residual = 0, No Iterations 0
DILUPBiCG: Solving for CO2, Initial residual = 0, Final residual = 0, No Iterations 0
DILUPBiCG: Solving for h, Initial residual = 7.83341e-07, Final residual = 7.83341e-07, No Iterations 0
min/max(T) = 358.241, 1499.98
DICPCG: Solving for p, Initial residual = 5.76649e-07, Final residual = 5.76649e-07, No Iterations 0
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
time step continuity errors : sum local = 7.65015e-07, global = 3.51658e-18, cumulative = -0.00201457
rho max/min : 2.50857 2.33323e-06
DICPCG: Solving for p, Initial residual = 5.76649e-07, Final residual = 5.76649e-07, No Iterations 0
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
time step continuity errors : sum local = 7.65015e-07, global = 3.58657e-18, cumulative = -0.00201457
rho max/min : 2.50857 2.33323e-06
ExecutionTime = 118.77 s ClockTime = 120 s

Courant Number mean: 6.95254e-05 max: 0.399999
deltaT = 9.51119e-12
.
.
.
saadouda likes this.
ghazal_1989 is offline   Reply With Quote

Reply

Thread Tools Search this Thread
Search this Thread:

Advanced Search
Display Modes

Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
[blockMesh] blockMesh with double grading. spwater OpenFOAM Meshing & Mesh Conversion 92 January 12, 2019 09:00
Compile problem ivanyao OpenFOAM Running, Solving & CFD 1 October 12, 2012 09:31
How to install CGNS under windows xp? lzgwhy Main CFD Forum 1 January 11, 2011 18:44
POSDAT problem piotka STAR-CD 4 June 12, 2009 08:43
DecomposePar links against liblamso0 with OpenMPI jens_klostermann OpenFOAM Bugs 11 June 28, 2007 17:51


All times are GMT -4. The time now is 06:33.