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FATAL ERROR: Max number of iterations exceeded |
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#1 |
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New Member
Henry
Join Date: May 2016
Posts: 15
Rep Power: 11 ![]() |
I've been having a lot of trouble tracing the source of this error. I know it happens in the thermoI.H file, but I can't trace what is calling that, or figure out any reason why this is happening.
The case i am running is a simple wedge (meshed with snappy hex mesh) inside a blockmesh region using rhoCentral foam. any help would be really appreciated this is the error log file Code:
/*---------------------------------------------------------------------------*\
| ========= | |
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
| \\ / O peration | Version: 3.0.1 |
| \\ / A nd | Web: www.OpenFOAM.org |
| \\/ M anipulation | |
\*---------------------------------------------------------------------------*/
Build : 3.0.1-119cac7e8750
Exec : rhoCentralFoam -parallel
Date : Jul 01 2016
Time : 12:54:38
Host : "cfd01"
PID : 30359
Case : /----/wedge15maxIterError
nProcs : 36
Slaves :
35
(
"cfd01.30360"
"cfd01.30361"
"cfd01.30362"
"cfd01.30363"
"cfd01.30364"
"cfd01.30365"
"cfd01.30366"
"cfd01.30367"
"cfd01.30368"
"cfd01.30369"
"cfd01.30370"
"cfd02.26571"
"cfd02.26572"
"cfd02.26573"
"cfd02.26574"
"cfd02.26575"
"cfd02.26576"
"cfd02.26577"
"cfd02.26578"
"cfd02.26579"
"cfd02.26580"
"cfd02.26581"
"cfd02.26582"
"cfd03.29133"
"cfd03.29134"
"cfd03.29135"
"cfd03.29136"
"cfd03.29137"
"cfd03.29138"
"cfd03.29139"
"cfd03.29140"
"cfd03.29141"
"cfd03.29142"
"cfd03.29143"
"cfd03.29144"
)
Pstream initialized with:
floatTransfer : 0
nProcsSimpleSum : 0
commsType : nonBlocking
polling iterations : 0
sigFpe : Enabling floating point exception trapping (FOAM_SIGFPE).
fileModificationChecking : Monitoring run-time modified files using timeStampMaster
allowSystemOperations : Allowing user-supplied system call operations
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
Create time
Create mesh for time = 0
Reading thermophysical properties
Selecting thermodynamics package
{
type hePsiThermo;
mixture pureMixture;
transport const;
thermo hConst;
equationOfState perfectGas;
specie specie;
energy sensibleInternalEnergy;
}
Reading field U
Creating turbulence model
Selecting turbulence model type laminar
fluxScheme: Kurganov
Starting time loop
Mean and max Courant Numbers = 0.00521015 0.119072
deltaT = 2.4e-06
Time = 2.4e-06
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
diagonal: Solving for rhoUx, Initial residual = 0, Final residual = 0, No Iterations 0
diagonal: Solving for rhoUy, Initial residual = 0, Final residual = 0, No Iterations 0
diagonal: Solving for rhoUz, Initial residual = 0, Final residual = 0, No Iterations 0
smoothSolver: Solving for Ux, Initial residual = 0.999285, Final residual = 0.00389594, No Iterations 5
smoothSolver: Solving for Uy, Initial residual = 0.999999, Final residual = 8.69665e-17, No Iterations 5
smoothSolver: Solving for Uz, Initial residual = 1, Final residual = 8.81879e-17, No Iterations 5
diagonal: Solving for rhoE, Initial residual = 0, Final residual = 0, No Iterations 0
smoothSolver: Solving for e, Initial residual = 1.46977e-11, Final residual = 1.46977e-11, No Iterations 0
ExecutionTime = 0.68 s ClockTime = 1 s
Mean and max Courant Numbers = 0.00625242 0.142579
deltaT = 2.88e-06
Time = 5.28e-06
diagonal: Solving for rho, Initial residual = 0, Final residual = 0, No Iterations 0
diagonal: Solving for rhoUx, Initial residual = 0, Final residual = 0, No Iterations 0
diagonal: Solving for rhoUy, Initial residual = 0, Final residual = 0, No Iterations 0
diagonal: Solving for rhoUz, Initial residual = 0, Final residual = 0, No Iterations 0
smoothSolver: Solving for Ux, Initial residual = 6.23273e-10, Final residual = 6.23273e-10, No Iterations 0
smoothSolver: Solving for Uy, Initial residual = 1.24042e-05, Final residual = 6.5351e-18, No Iterations 5
smoothSolver: Solving for Uz, Initial residual = 0.00028774, Final residual = 4.85118e-17, No Iterations 5
diagonal: Solving for rhoE, Initial residual = 0, Final residual = 0, No Iterations 0
smoothSolver: Solving for e, Initial residual = 5.7298e-12, Final residual = 5.7298e-12, No Iterations 0
[0] [1]
[1]
[1] --> FOAM FATAL ERROR:
[1] Maximum number of iterations exceeded
[1]
[1] From function Foam::scalar Foam::species::thermo<Thermo, Type>::T(Foam::scalar, Foam::scalar, Foam::scalar, Foam::scalar (Foam::species::thermo<Thermo, Type>::*)(Foam::scalar, Foam::scalar)const, Foam::scalar (Foam::species::thermo<Thermo, Type>::*)(Foam::scalar, Foam::scalar)const, Foam::scalar (Foam::species::thermo<Thermo, Type>::*)(Foam::scalar)const) const [with Thermo = Foam::hConstThermo<Foam::perfectGas<Foam::specie> >; Type = Foam::sensibleInternalEnergy; Foam::scalar = double; Foam::species::thermo<Thermo, Type> = Foam::species::thermo<Foam::hConstThermo<Foam::perfectGas<Foam::specie> >, Foam::sensibleInternalEnergy>]
[1] in file /home/openfoam/OpenFOAM/OpenFOAM-3.0.1/src/thermophysicalModels/specie/lnInclude/thermoI.H at line 66.
[1]
FOAM parallel run aborting
[1]
[2]
[2]
[2] --> FOAM FATAL ERROR: [3]
[3]
[3] --> FOAM FATAL ERROR:
[3] Maximum number of iterations exceeded
[3]
[3] From function Foam::scalar Foam::species::thermo<Thermo, Type>::T(Foam::scalar, Foam::scalar, Foam::scalar, Foam::scalar (Foam::species::thermo<Thermo, Type>::*)(Foam::scalar, Foam::scalar)const, Foam::scalar (Foam::species::thermo<Thermo, Type>::*)(Foam::scalar, Foam::scalar)const, Foam::scalar (Foam::species::thermo<Thermo, Type>::*)(Foam::scalar)const) const [with Thermo = Foam::hConstThermo<Foam::perfectGas<Foam::specie> >; Type = Foam::sensibleInternalEnergy; Foam::scalar = double; Foam::species::thermo<Thermo, Type> = Foam::species::thermo<Foam::hConstThermo<Foam::perfectGas<Foam::specie> >, Foam::sensibleInternalEnergy>]
[3] in file /home/openfoam/OpenFOAM/OpenFOAM-3.0.1/src/thermophysicalModels/specie/lnInclude/thermoI.H at line 66[7]
[7]
[7] --> FOAM FATAL ERROR:
[7] Maximum number of iterations exceeded
[7]
.
p: Code:
dimensions [1 -1 -2 0 0 0 0];
internalField uniform 18822.7;
boundaryField
{
inlet
{
type fixedValue;
value uniform 18822.7;
}
outlet
{
type zeroGradient;
}
airplane
{
type zeroGradient;
}
bottom
{
type zeroGradient;
}
top
{
type zeroGradient;
}
symmetry
{
type symmetryPlane;
}
left
{
type zeroGradient;
}
defaultFaces
{
type zeroGradient;
}
}
Code:
dimensions [0 0 0 1 0 0 0];
internalField uniform 216.65;
boundaryField
{
inlet
{
type fixedValue;
value uniform 216.65;
}
outlet
{
type zeroGradient;
}
airplane
{
type zeroGradient;
}
bottom
{
type zeroGradient;
}
top
{
type zeroGradient;
}
left
{
type zeroGradient;
}
symmetry
{
type symmetryPlane;
}
defaultFaces
{
type zeroGradient;
}
}
Code:
dimensions [0 1 -1 0 0 0 0];
internalField uniform (400 0 0); //(246.933 0 0);
boundaryField
{
inlet
{
type fixedValue;
value uniform (400 0 0); //(246.933 0 0);
}
outlet
{
type zeroGradient;
}
airplane
{
type slip;
}
bottom
{
type zeroGradient;
}
top
{
type zeroGradient;
}
left
{
type zeroGradient;
}
symmetry
{
type symmetryPlane;
}
defaultFaces
{
type zeroGradient;
}
}
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#2 |
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New Member
Henry
Join Date: May 2016
Posts: 15
Rep Power: 11 ![]() |
Also, I changed the boundary conditions to supersonicFreestream and waveTransmissive in hopes that that would help, but i am getting the same problem.
I have my entire post-run case directory on dropbox, with the error located in the log.rho file https://www.dropbox.com/sh/7fvzzazmx...liXvZj0ga?dl=0 Does anyone have any ideas what the problem is? |
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#3 | |
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New Member
Hao Li
Join Date: May 2017
Posts: 7
Rep Power: 10 ![]() |
Quote:
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#4 |
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New Member
Fuad Hasibul Hasan
Join Date: Feb 2022
Location: Dhaka, Bangladesh
Posts: 7
Rep Power: 5 ![]() |
Hi,
Have you solved this issue? I'm facing a similar error. I've been working on this error for more than a week but could not solve this yet. Please share if you did. In my observation after trying a lot of things is that they are may be a unit problem of the initial and boundary conditions and thermophysical properties. The tutorial cases use the normalized parameters and as soon as I change them to S.I. units like here it causes this error. |
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