[yglovella]

Hi everybody

I am trying to adapt simplifiedSiwek tutorial case to a pulverized coal combustion application. But, after setting up everything I got the following error. I am using OpenFOAM/9-foss-2021a in a HPC facility.
Any help will be appreciated

/*---------------------------------------------------------------------------*\
========= |
\\ / F ield | OpenFOAM: The Open Source CFD Toolbox
\\ / O peration | Website: https://openfoam.org
\\ / A nd | Version: 9
\\/ M anipulation |
\*---------------------------------------------------------------------------*/
Build : 9
Exec : reactingFoam -parallel
Date : Feb 16 2023
Time : 05:49:52
Host : "nodo20.uclv.hpc.cu"
PID : 69404
I/O : uncollated
Case : /users/uclv_yanielg/CRIEPI_Jet_Flame_Burner
nProcs : 4
Slaves :
3
(
"nodo20.uclv.hpc.cu.69405"
"nodo20.uclv.hpc.cu.69406"
"nodo20.uclv.hpc.cu.69407"
)

Pstream initialised 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 (fileModificationSkew 10)
allowSystemOperations : Allowing user-supplied system call operations

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

Create mesh for time = 0


PIMPLE: No convergence criteria found


PIMPLE: Operating solver in transient mode with 1 outer corrector
PIMPLE: Operating solver in PISO mode


Reading thermophysical properties

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

Reading field U

Reading/calculating face flux field phi

Creating turbulence model.

Selecting turbulence model type LES
Selecting LES turbulence model kEqn
Selecting LES delta type cubeRootVol
bounding k, min: 0 max: 2e-05 average: 0
LES
{
model kEqn;
turbulence on;
printCoeffs on;
delta cubeRootVol;
cubeRootVolCoeffs
{
deltaCoeff 1;
}
PrandtlCoeffs
{
delta cubeRootVol;
cubeRootVolCoeffs
{
deltaCoeff 1;
}
smoothCoeffs
{
delta cubeRootVol;
cubeRootVolCoeffs
{
deltaCoeff 1;
}
maxDeltaRatio 1.1;
}
Cdelta 0.158;
}
vanDriestCoeffs
{
delta cubeRootVol;
cubeRootVolCoeffs
{
deltaCoeff 1;
}
smoothCoeffs
{
delta cubeRootVol;
cubeRootVolCoeffs
{
deltaCoeff 1;
}
maxDeltaRatio 1.1;
}
Aplus 26;
Cdelta 0.158;
}
smoothCoeffs
{
delta cubeRootVol;
cubeRootVolCoeffs
{
deltaCoeff 1;
}
maxDeltaRatio 1.1;
}
Ce 1.048;
Ck 0.094;
}

Creating thermophysical transport model

Selecting thermophysical transport type LES
Selecting default LES thermophysical transport model unityLewisEddyDiffusivity
Creating reaction model

Selecting combustion model PaSR
Selecting chemistry solver
{
solver ode;
method standard;
}

standardChemistryModel: Number of species = 6 and reactions = 2
Selecting ODE solver seulex
using integrated reaction rate
Creating field dpdt

Creating field kinetic energy K

No MRF models present

Creating fvModels from "constant/fvModels"

Selecting finite volume model type buoyancyForce
Name: buoyancyForce
Selecting finite volume model type clouds
Name: clouds
Selecting parcelCloud reactingMultiphaseCloud
Constructing particle forces
Selecting particle force sphereDrag
Selecting particle force gravity
Constructing cloud functions
none
Constructing particle injection models
Creating injector: model1
Selecting injection model manualInjection
Constructing 3-D injection
Selecting distribution model RosinRammler
Distribution min: 5e-06 max: 0.0005 mean: 5e-05
Selecting dispersion model stochasticDispersionRAS
Selecting patch interaction model standardWallInteraction
Selecting stochastic collision model none
Selecting surface film model none
Selecting U integration scheme Euler
Creating component thermo properties:
liquids - 1 components
solids - 3 components
Selecting heat transfer model RanzMarshall
Selecting composition model singleMixtureFraction
Selecting T integration scheme analytical
Selecting phase change model liquidEvaporation
Participating liquid species:
H2O
Selecting devolatilisation model constantRateDevolatilisation
Participating volatile species:
CH4: particle mass fraction = 0.127444
H2: particle mass fraction = 0.020889
CO2: particle mass fraction = 0.062667
Selecting surface reaction model COxidationKineticDiffusionLimitedRate
C(s): particle mass fraction = 0.659000048
Selecting parcelCloud thermoCloud
Constructing particle forces
Selecting particle force sphereDrag
Selecting particle force gravity
Constructing cloud functions
none
Constructing particle injection models
Creating injector: model1
Selecting injection model manualInjection
Constructing 3-D injection
Selecting distribution model RosinRammler
Distribution min: 5e-06 max: 0.000565 mean: 4.8e-05
Selecting dispersion model stochasticDispersionRAS
Selecting patch interaction model standardWallInteraction
Selecting stochastic collision model none
Selecting surface film model none
Selecting U integration scheme Euler
Creating component thermo properties:
liquids - 1 components
solids - 3 components
Selecting heat transfer model RanzMarshall
Selecting composition model singlePhaseMixture
Selecting T integration scheme analytical
Selecting finite volume model type radiation
Name: radiation
Selecting radiationModel P1
Selecting absorptionEmissionModel binary
Selecting absorptionEmissionModel constant
Selecting absorptionEmissionModel cloud
Selecting scatterModel cloud
Creating fvConstraints from "system/fvConstraints"

Selecting finite volume constraint type fixedTemperatureConstraint
Name: source1
- selecting cells using cellSet ignitionCells
- selected 1 cell(s) with volume 2.681904768e-12
[3] #0 Foam::error:rintStack(Foam::Ostream&)[0] #0 Foam::error:rintStack(Foam::Ostream&)[1] #0 Foam::error:rintStack(Foam::Ostream&)[2] #0 Foam::error:rintStack(Foam::Ostream&)[1676526618.105599] [nodo20:69406:0] ib_md.c:1161 UCX WARN IB: ibv_fork_init() was disabled or failed, yet a fork() has been issued.
[1676526618.105637] [nodo20:69406:0] ib_md.c:1162 UCX WARN IB: data corruption might occur when using registered memory.
-------------------------