BaramFlow: Advanced sections in Initialisation not showing/working
Quote from Yash R on April 24, 2026, 6:35 pmWhen I try to view Advanced sections in the Initialization tab of BaramFlow, there is nothing visible even though the eye icon is on the "show" position as seen in the attached pictures. Additionally when trying to initialise the case with volume fractions in the sections to be 1 while the volume fractions everywhere else to be 0, the calculation crashes and terminates. I have tried using the adaptive timestep but that crashes too (Courant number of 0.5).
To be clear, I am trying to do a Free Surface VOF simulation of slurry moving through a system where some chambers are already partially filled with slurry and the rest is supposed to be air.
Any help in this matter would be greatly appreciated.
Additionally I am adding in the full console logs below just in case it proves to be helpful.
/*---------------------------------------------------------------------------*\
| ========= | |
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
| \\ / O peration | Version: 2412 |
| \\ / A nd | Website: http://www.openfoam.com |
| \\/ M anipulation | |
\*---------------------------------------------------------------------------*/
Build : 70abf28e-20260105 OPENFOAM=2412 version=v2412
Arch : "LSB;label=32;scalar=64"
Exec : T:\Baram\solvers\openfoam\bin\interFoam -parallel
Date : Apr 24 2026
Time : 13:13:31
Host : YASH-SCX
PID : 11860
I/O : uncollated
Case : T:/New Chapter/case
nProcs : 24
Hosts :
(
(YASH-SCX 24)
)
Pstream initialized with:
floatTransfer : false
maxCommsSize : 0
nProcsSimpleSum : 0
nonBlockingExchange: 0 (tuning: 0)
exchange algorithm : 0
commsType : nonBlocking
polling iterations : 0
trapFpe: Floating point exception trapping enabled (FOAM_SIGFPE).
fileModificationChecking : Monitoring run-time modified files using timeStampMaster (fileModificationSkew 0, maxFileModificationPolls 20)
allowSystemOperations : Allowing user-supplied system call operations
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
Create time
Create mesh for time = 0
PIMPLE: max iterations = 2
field p : relTol 0.05, tolerance 0.0001
field p_rgh : relTol 0.05, tolerance 0.0001
field U : relTol 0.05, tolerance 0.0001
field h : relTol 0.05, tolerance 0.001
field "(k|epsilon|omega|nuTilda)" : relTol 0.05, tolerance 0.0001
field "alpha.*" : relTol 0.05, tolerance 0.0001
field scalar : relTol 0.05, tolerance 0.001
Reading field p_rgh
Reading field U
Reading/calculating face flux field phi
Reading transportProperties
Selecting incompressible transport model Newtonian
Selecting incompressible transport model Newtonian
Selecting turbulence model type RAS
Selecting RAS turbulence model kEpsilon
kEpsilonCoeffs
{
Prt 0.85;
Sct 0.7;
Cmu 0.09;
C1 1.44;
C2 1.92;
C3 0;
sigmak 1;
sigmaEps 1.3;
}
Reading g
Reading hRef
Calculating field g.h
No MRF models present
No finite volume options present
GAMGPCG: Solving for pcorr, Initial residual = 1, Final residual = 0.0950523, No Iterations 4
GAMGPCG: Solving for pcorr, Initial residual = 0.000678481, Final residual = 1.46718e-05, No Iterations 1
time step continuity errors : sum local = 8.13146e-06, global = -1.77676e-07, cumulative = -1.77676e-07
Courant Number mean: 0.0136551 max: 0.722913
Starting time loop
Courant Number mean: 0.0136551 max: 0.722913
Interface Courant Number mean: 0 max: 0
Time = 0.5
PIMPLE: iteration 1
smoothSolver: Solving for alpha.SlurryLiquid, Initial residual = 1, Final residual = 3.87061e-12, No Iterations 3
Phase-1 volume fraction = 1.12195e-05 Min(alpha.SlurryLiquid) = 0 Max(alpha.SlurryLiquid) = 1
MULES: Correcting alpha.SlurryLiquid
Phase-1 volume fraction = 1.12195e-05 Min(alpha.SlurryLiquid) = -6.88244e-64 Max(alpha.SlurryLiquid) = 1
smoothSolver: Solving for alpha.SlurryLiquid, Initial residual = 0.0771706, Final residual = 3.72405e-09, No Iterations 2
Phase-1 volume fraction = 2.24389e-05 Min(alpha.SlurryLiquid) = 0 Max(alpha.SlurryLiquid) = 1
Applying the previous iteration compression flux
MULES: Correcting alpha.SlurryLiquid
MULES: Correcting alpha.SlurryLiquid
Phase-1 volume fraction = 2.24389e-05 Min(alpha.SlurryLiquid) = -1.54005e-32 Max(alpha.SlurryLiquid) = 1
DILUPBiCGStab: Solving for Ux, Initial residual = 1, Final residual = 3.05495e-08, No Iterations 1
DILUPBiCGStab: Solving for Uy, Initial residual = 1, Final residual = 4.5319e-08, No Iterations 1
DILUPBiCGStab: Solving for Uz, Initial residual = 1, Final residual = 2.88777e-08, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 1, Final residual = 0.019572, No Iterations 3
GAMGPCG: Solving for p_rgh, Initial residual = 0.000669841, Final residual = 1.37425e-05, No Iterations 1
time step continuity errors : sum local = 0.0242588, global = 0.000158723, cumulative = 0.000158545
GAMGPCG: Solving for p_rgh, Initial residual = 0.00513927, Final residual = 0.000281166, No Iterations 2
GAMGPCG: Solving for p_rgh, Initial residual = 0.000496577, Final residual = 1.63621e-05, No Iterations 1
time step continuity errors : sum local = 0.0317801, global = -0.00011495, cumulative = 4.35955e-05
GAMGPCG: Solving for p_rgh, Initial residual = 0.76231, Final residual = 0.00690857, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 0.00123408, Final residual = 4.4164e-05, No Iterations 2
time step continuity errors : sum local = 1.55181, global = 0.051071, cumulative = 0.0511146
GAMGPCG: Solving for p_rgh, Initial residual = 0.999982, Final residual = 0.00810726, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 0.0011329, Final residual = 4.08253e-05, No Iterations 2
time step continuity errors : sum local = 717947, global = 26370.3, cumulative = 26370.4
DILUPBiCGStab: Solving for epsilon, Initial residual = 1, Final residual = 6.53664e-06, No Iterations 1
DILUPBiCGStab: Solving for k, Initial residual = 1, Final residual = 6.5885e-06, No Iterations 1
PIMPLE: iteration 2
smoothSolver: Solving for alpha.SlurryLiquid, Initial residual = 0.0026161, Final residual = 0.000272147, No Iterations 10
Phase-1 volume fraction = -0.0135824 Min(alpha.SlurryLiquid) = -63700.6 Max(alpha.SlurryLiquid) = 1
Applying the previous iteration compression flux
MULES: Correcting alpha.SlurryLiquid
MULES: Correcting alpha.SlurryLiquid
Phase-1 volume fraction = -0.0135824 Min(alpha.SlurryLiquid) = -49630.4 Max(alpha.SlurryLiquid) = 7313.63
smoothSolver: Solving for alpha.SlurryLiquid, Initial residual = 0.120554, Final residual = 0.000189834, No Iterations 10
Phase-1 volume fraction = -1.5184 Min(alpha.SlurryLiquid) = -5.90608e+06 Max(alpha.SlurryLiquid) = 525671
Applying the previous iteration compression flux
MULES: Correcting alpha.SlurryLiquid
MULES: Correcting alpha.SlurryLiquid
Phase-1 volume fraction = -1.5184 Min(alpha.SlurryLiquid) = -2.8011e+07 Max(alpha.SlurryLiquid) = 2.71259e+07
DILUPBiCGStab: Solving for Ux, Initial residual = 0.74802, Final residual = 0.000298879, No Iterations 1
DILUPBiCGStab: Solving for Uy, Initial residual = 0.27856, Final residual = 0.00132837, No Iterations 1
DILUPBiCGStab: Solving for Uz, Initial residual = 0.748282, Final residual = 0.000259006, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 0.420671, Final residual = 0.0156574, No Iterations 3
GAMGPCG: Solving for p_rgh, Initial residual = 2.83824e-12, Final residual = 2.60308e-13, No Iterations 1
time step continuity errors : sum local = 4.48706e+06, global = -471803, cumulative = -445433
GAMGPCG: Solving for p_rgh, Initial residual = 3.40887e-11, Final residual = 2.34197e-12, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 7.16186e-12, Final residual = 1.85474e-13, No Iterations 4
time step continuity errors : sum local = 1.88838e+06, global = 133678, cumulative = -311755
GAMGPCG: Solving for p_rgh, Initial residual = 0.33253, Final residual = 0.000689595, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 0.00781207, Final residual = 5.69402e-05, No Iterations 1
time step continuity errors : sum local = 1.9138e+14, global = -4.03591e+13, cumulative = -4.03591e+13
GAMGPCG: Solving for p_rgh, Initial residual = 1, Final residual = 0.00100142, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 0.00730696, Final residual = 5.99409e-05, No Iterations 1
time step continuity errors : sum local = 3.66867e+35, global = -2.1585e+35, cumulative = -2.1585e+35
DILUPBiCGStab: Solving for epsilon, Initial residual = 1, Final residual = 0.00206277, No Iterations 1
DILUPBiCGStab: Solving for k, Initial residual = 1, Final residual = 0.00205136, No Iterations 1
bounding k, min: -419.951 max: 8.23046e+42 average: 3.00549e+37
PIMPLE: not converged within 2 iterations
ExecutionTime = 39.126 s ClockTime = 39 s
--> FOAM Warning :
From virtual bool Foam::functionObjects::fieldSelection::checkSelection()
in file functionObjects/fieldSelections/fieldSelection/fieldSelection.C at line 179
Field alpha.air not found
--> FOAM Warning :
From virtual bool Foam::functionObjects::solverFieldSelection::updateSelection()
in file functionObjects/fieldSelections/solverFieldSelection/solverFieldSelection.C at line 82
Valid solver fields are: 5(U alpha.SlurryLiquid epsilon k p_rgh)Courant Number mean: 1.1638e+39 max: 1.31756e+45
Interface Courant Number mean: 2.19109e+13 max: 1.15995e+18
Time = 1
PIMPLE: iteration 1
smoothSolver: Solving for alpha.SlurryLiquid, Initial residual = 2.95045e-20, Final residual = 3.44542e-21, No Iterations 1
Phase-1 volume fraction = 0.16027 Min(alpha.SlurryLiquid) = -2.02414e+06 Max(alpha.SlurryLiquid) = 8.05633e+06
Applying the previous iteration compression flux
MULES: Correcting alpha.SlurryLiquid
MULES: Correcting alpha.SlurryLiquid
Phase-1 volume fraction = -30.3516 Min(alpha.SlurryLiquid) = -3.8029e+22 Max(alpha.SlurryLiquid) = 1.0112e+23
smoothSolver: Solving for alpha.SlurryLiquid, Initial residual = 9.69247e-19, Final residual = 1.19896e-19, No Iterations 1
Phase-1 volume fraction = -3.45942e+16 Min(alpha.SlurryLiquid) = -1.04433e+22 Max(alpha.SlurryLiquid) = 5.63891e+21
Applying the previous iteration compression flux
MULES: Correcting alpha.SlurryLiquid
MULES: Correcting alpha.SlurryLiquid
Phase-1 volume fraction = 9.77606e+36 Min(alpha.SlurryLiquid) = -3.08391e+57 Max(alpha.SlurryLiquid) = 7.50166e+57
DILUPBiCGStab: Solving for Ux, Initial residual = 2.04715e-16, Final residual = 3.24368e-19, No Iterations 1
DILUPBiCGStab: Solving for Uy, Initial residual = 3.73104e-18, Final residual = 3.17586e-21, No Iterations 1
DILUPBiCGStab: Solving for Uz, Initial residual = 2.09271e-17, Final residual = 1.93408e-20, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 1, Final residual = 0.0142094, No Iterations 2
GAMGPCG: Solving for p_rgh, Initial residual = 6.03829e-20, Final residual = 9.04518e-22, No Iterations 1
time step continuity errors : sum local = 1.32053e+36, global = -1.01862e+35, cumulative = -3.17712e+35
GAMGPCG: Solving for p_rgh, Initial residual = 1.29657e-14, Final residual = 1.65944e-16, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 1.40866e-16, Final residual = 2.63519e-17, No Iterations 1
time step continuity errors : sum local = 1.83322e+40, global = -5.33755e+39, cumulative = -5.33787e+39
GAMGPCG: Solving for p_rgh, Initial residual = 1, Final residual = 0.0118204, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 0.00145539, Final residual = 0.000125225, No Iterations 1
time step continuity errors : sum local = 1.37598e+61, global = 2.73327e+60, cumulative = 2.73327e+60
GAMGPCG: Solving for p_rgh, Initial residual = 1, Final residual = 0.0201398, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 0.00190933, Final residual = 6.04856e-05, No Iterations 2
time step continuity errors : sum local = 1.14254e+105, global = 1.14168e+104, cumulative = 1.14168e+104
job aborted:
[ranks] message
[0-23] process exited without calling finalize
---- error analysis -----
[0-23] on YASH-SCX
T:\Baram\solvers\openfoam\bin\interFoam ended prematurely and may have crashed. exit code 3
---- error analysis -----
When I try to view Advanced sections in the Initialization tab of BaramFlow, there is nothing visible even though the eye icon is on the "show" position as seen in the attached pictures. Additionally when trying to initialise the case with volume fractions in the sections to be 1 while the volume fractions everywhere else to be 0, the calculation crashes and terminates. I have tried using the adaptive timestep but that crashes too (Courant number of 0.5).
To be clear, I am trying to do a Free Surface VOF simulation of slurry moving through a system where some chambers are already partially filled with slurry and the rest is supposed to be air.
Any help in this matter would be greatly appreciated.
Additionally I am adding in the full console logs below just in case it proves to be helpful.
/*---------------------------------------------------------------------------*\
| ========= | |
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
| \\ / O peration | Version: 2412 |
| \\ / A nd | Website: http://www.openfoam.com |
| \\/ M anipulation | |
\*---------------------------------------------------------------------------*/
Build : 70abf28e-20260105 OPENFOAM=2412 version=v2412
Arch : "LSB;label=32;scalar=64"
Exec : T:\Baram\solvers\openfoam\bin\interFoam -parallel
Date : Apr 24 2026
Time : 13:13:31
Host : YASH-SCX
PID : 11860
I/O : uncollated
Case : T:/New Chapter/case
nProcs : 24
Hosts :
(
(YASH-SCX 24)
)
Pstream initialized with:
floatTransfer : false
maxCommsSize : 0
nProcsSimpleSum : 0
nonBlockingExchange: 0 (tuning: 0)
exchange algorithm : 0
commsType : nonBlocking
polling iterations : 0
trapFpe: Floating point exception trapping enabled (FOAM_SIGFPE).
fileModificationChecking : Monitoring run-time modified files using timeStampMaster (fileModificationSkew 0, maxFileModificationPolls 20)
allowSystemOperations : Allowing user-supplied system call operations
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
Create time
Create mesh for time = 0
PIMPLE: max iterations = 2
field p : relTol 0.05, tolerance 0.0001
field p_rgh : relTol 0.05, tolerance 0.0001
field U : relTol 0.05, tolerance 0.0001
field h : relTol 0.05, tolerance 0.001
field "(k|epsilon|omega|nuTilda)" : relTol 0.05, tolerance 0.0001
field "alpha.*" : relTol 0.05, tolerance 0.0001
field scalar : relTol 0.05, tolerance 0.001
Reading field p_rgh
Reading field U
Reading/calculating face flux field phi
Reading transportProperties
Selecting incompressible transport model Newtonian
Selecting incompressible transport model Newtonian
Selecting turbulence model type RAS
Selecting RAS turbulence model kEpsilon
kEpsilonCoeffs
{
Prt 0.85;
Sct 0.7;
Cmu 0.09;
C1 1.44;
C2 1.92;
C3 0;
sigmak 1;
sigmaEps 1.3;
}
Reading g
Reading hRef
Calculating field g.h
No MRF models present
No finite volume options present
GAMGPCG: Solving for pcorr, Initial residual = 1, Final residual = 0.0950523, No Iterations 4
GAMGPCG: Solving for pcorr, Initial residual = 0.000678481, Final residual = 1.46718e-05, No Iterations 1
time step continuity errors : sum local = 8.13146e-06, global = -1.77676e-07, cumulative = -1.77676e-07
Courant Number mean: 0.0136551 max: 0.722913
Starting time loop
Courant Number mean: 0.0136551 max: 0.722913
Interface Courant Number mean: 0 max: 0
Time = 0.5
PIMPLE: iteration 1
smoothSolver: Solving for alpha.SlurryLiquid, Initial residual = 1, Final residual = 3.87061e-12, No Iterations 3
Phase-1 volume fraction = 1.12195e-05 Min(alpha.SlurryLiquid) = 0 Max(alpha.SlurryLiquid) = 1
MULES: Correcting alpha.SlurryLiquid
Phase-1 volume fraction = 1.12195e-05 Min(alpha.SlurryLiquid) = -6.88244e-64 Max(alpha.SlurryLiquid) = 1
smoothSolver: Solving for alpha.SlurryLiquid, Initial residual = 0.0771706, Final residual = 3.72405e-09, No Iterations 2
Phase-1 volume fraction = 2.24389e-05 Min(alpha.SlurryLiquid) = 0 Max(alpha.SlurryLiquid) = 1
Applying the previous iteration compression flux
MULES: Correcting alpha.SlurryLiquid
MULES: Correcting alpha.SlurryLiquid
Phase-1 volume fraction = 2.24389e-05 Min(alpha.SlurryLiquid) = -1.54005e-32 Max(alpha.SlurryLiquid) = 1
DILUPBiCGStab: Solving for Ux, Initial residual = 1, Final residual = 3.05495e-08, No Iterations 1
DILUPBiCGStab: Solving for Uy, Initial residual = 1, Final residual = 4.5319e-08, No Iterations 1
DILUPBiCGStab: Solving for Uz, Initial residual = 1, Final residual = 2.88777e-08, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 1, Final residual = 0.019572, No Iterations 3
GAMGPCG: Solving for p_rgh, Initial residual = 0.000669841, Final residual = 1.37425e-05, No Iterations 1
time step continuity errors : sum local = 0.0242588, global = 0.000158723, cumulative = 0.000158545
GAMGPCG: Solving for p_rgh, Initial residual = 0.00513927, Final residual = 0.000281166, No Iterations 2
GAMGPCG: Solving for p_rgh, Initial residual = 0.000496577, Final residual = 1.63621e-05, No Iterations 1
time step continuity errors : sum local = 0.0317801, global = -0.00011495, cumulative = 4.35955e-05
GAMGPCG: Solving for p_rgh, Initial residual = 0.76231, Final residual = 0.00690857, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 0.00123408, Final residual = 4.4164e-05, No Iterations 2
time step continuity errors : sum local = 1.55181, global = 0.051071, cumulative = 0.0511146
GAMGPCG: Solving for p_rgh, Initial residual = 0.999982, Final residual = 0.00810726, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 0.0011329, Final residual = 4.08253e-05, No Iterations 2
time step continuity errors : sum local = 717947, global = 26370.3, cumulative = 26370.4
DILUPBiCGStab: Solving for epsilon, Initial residual = 1, Final residual = 6.53664e-06, No Iterations 1
DILUPBiCGStab: Solving for k, Initial residual = 1, Final residual = 6.5885e-06, No Iterations 1
PIMPLE: iteration 2
smoothSolver: Solving for alpha.SlurryLiquid, Initial residual = 0.0026161, Final residual = 0.000272147, No Iterations 10
Phase-1 volume fraction = -0.0135824 Min(alpha.SlurryLiquid) = -63700.6 Max(alpha.SlurryLiquid) = 1
Applying the previous iteration compression flux
MULES: Correcting alpha.SlurryLiquid
MULES: Correcting alpha.SlurryLiquid
Phase-1 volume fraction = -0.0135824 Min(alpha.SlurryLiquid) = -49630.4 Max(alpha.SlurryLiquid) = 7313.63
smoothSolver: Solving for alpha.SlurryLiquid, Initial residual = 0.120554, Final residual = 0.000189834, No Iterations 10
Phase-1 volume fraction = -1.5184 Min(alpha.SlurryLiquid) = -5.90608e+06 Max(alpha.SlurryLiquid) = 525671
Applying the previous iteration compression flux
MULES: Correcting alpha.SlurryLiquid
MULES: Correcting alpha.SlurryLiquid
Phase-1 volume fraction = -1.5184 Min(alpha.SlurryLiquid) = -2.8011e+07 Max(alpha.SlurryLiquid) = 2.71259e+07
DILUPBiCGStab: Solving for Ux, Initial residual = 0.74802, Final residual = 0.000298879, No Iterations 1
DILUPBiCGStab: Solving for Uy, Initial residual = 0.27856, Final residual = 0.00132837, No Iterations 1
DILUPBiCGStab: Solving for Uz, Initial residual = 0.748282, Final residual = 0.000259006, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 0.420671, Final residual = 0.0156574, No Iterations 3
GAMGPCG: Solving for p_rgh, Initial residual = 2.83824e-12, Final residual = 2.60308e-13, No Iterations 1
time step continuity errors : sum local = 4.48706e+06, global = -471803, cumulative = -445433
GAMGPCG: Solving for p_rgh, Initial residual = 3.40887e-11, Final residual = 2.34197e-12, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 7.16186e-12, Final residual = 1.85474e-13, No Iterations 4
time step continuity errors : sum local = 1.88838e+06, global = 133678, cumulative = -311755
GAMGPCG: Solving for p_rgh, Initial residual = 0.33253, Final residual = 0.000689595, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 0.00781207, Final residual = 5.69402e-05, No Iterations 1
time step continuity errors : sum local = 1.9138e+14, global = -4.03591e+13, cumulative = -4.03591e+13
GAMGPCG: Solving for p_rgh, Initial residual = 1, Final residual = 0.00100142, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 0.00730696, Final residual = 5.99409e-05, No Iterations 1
time step continuity errors : sum local = 3.66867e+35, global = -2.1585e+35, cumulative = -2.1585e+35
DILUPBiCGStab: Solving for epsilon, Initial residual = 1, Final residual = 0.00206277, No Iterations 1
DILUPBiCGStab: Solving for k, Initial residual = 1, Final residual = 0.00205136, No Iterations 1
bounding k, min: -419.951 max: 8.23046e+42 average: 3.00549e+37
PIMPLE: not converged within 2 iterations
ExecutionTime = 39.126 s ClockTime = 39 s
--> FOAM Warning :
From virtual bool Foam::functionObjects::fieldSelection::checkSelection()
in file functionObjects/fieldSelections/fieldSelection/fieldSelection.C at line 179
Field alpha.air not found
--> FOAM Warning :
From virtual bool Foam::functionObjects::solverFieldSelection::updateSelection()
in file functionObjects/fieldSelections/solverFieldSelection/solverFieldSelection.C at line 82
Valid solver fields are: 5(U alpha.SlurryLiquid epsilon k p_rgh)Courant Number mean: 1.1638e+39 max: 1.31756e+45
Interface Courant Number mean: 2.19109e+13 max: 1.15995e+18
Time = 1
PIMPLE: iteration 1
smoothSolver: Solving for alpha.SlurryLiquid, Initial residual = 2.95045e-20, Final residual = 3.44542e-21, No Iterations 1
Phase-1 volume fraction = 0.16027 Min(alpha.SlurryLiquid) = -2.02414e+06 Max(alpha.SlurryLiquid) = 8.05633e+06
Applying the previous iteration compression flux
MULES: Correcting alpha.SlurryLiquid
MULES: Correcting alpha.SlurryLiquid
Phase-1 volume fraction = -30.3516 Min(alpha.SlurryLiquid) = -3.8029e+22 Max(alpha.SlurryLiquid) = 1.0112e+23
smoothSolver: Solving for alpha.SlurryLiquid, Initial residual = 9.69247e-19, Final residual = 1.19896e-19, No Iterations 1
Phase-1 volume fraction = -3.45942e+16 Min(alpha.SlurryLiquid) = -1.04433e+22 Max(alpha.SlurryLiquid) = 5.63891e+21
Applying the previous iteration compression flux
MULES: Correcting alpha.SlurryLiquid
MULES: Correcting alpha.SlurryLiquid
Phase-1 volume fraction = 9.77606e+36 Min(alpha.SlurryLiquid) = -3.08391e+57 Max(alpha.SlurryLiquid) = 7.50166e+57
DILUPBiCGStab: Solving for Ux, Initial residual = 2.04715e-16, Final residual = 3.24368e-19, No Iterations 1
DILUPBiCGStab: Solving for Uy, Initial residual = 3.73104e-18, Final residual = 3.17586e-21, No Iterations 1
DILUPBiCGStab: Solving for Uz, Initial residual = 2.09271e-17, Final residual = 1.93408e-20, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 1, Final residual = 0.0142094, No Iterations 2
GAMGPCG: Solving for p_rgh, Initial residual = 6.03829e-20, Final residual = 9.04518e-22, No Iterations 1
time step continuity errors : sum local = 1.32053e+36, global = -1.01862e+35, cumulative = -3.17712e+35
GAMGPCG: Solving for p_rgh, Initial residual = 1.29657e-14, Final residual = 1.65944e-16, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 1.40866e-16, Final residual = 2.63519e-17, No Iterations 1
time step continuity errors : sum local = 1.83322e+40, global = -5.33755e+39, cumulative = -5.33787e+39
GAMGPCG: Solving for p_rgh, Initial residual = 1, Final residual = 0.0118204, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 0.00145539, Final residual = 0.000125225, No Iterations 1
time step continuity errors : sum local = 1.37598e+61, global = 2.73327e+60, cumulative = 2.73327e+60
GAMGPCG: Solving for p_rgh, Initial residual = 1, Final residual = 0.0201398, No Iterations 1
GAMGPCG: Solving for p_rgh, Initial residual = 0.00190933, Final residual = 6.04856e-05, No Iterations 2
time step continuity errors : sum local = 1.14254e+105, global = 1.14168e+104, cumulative = 1.14168e+104
job aborted:
[ranks] message
[0-23] process exited without calling finalize
---- error analysis -----
[0-23] on YASH-SCX
T:\Baram\solvers\openfoam\bin\interFoam ended prematurely and may have crashed. exit code 3
---- error analysis -----
Uploaded files:
Quote from bykima5230416a7 on April 26, 2026, 2:48 pmLooking at the log you posted, it appears the simulation diverged. Given that the volume fraction was around 1.12195e-5 at the start of the calculation, I suspect the problem might be that the initialization wasn’t performed correctly.
First, I think you should check in Paraview or [Results-Scaffolds-Graphics] to see if the value of alpha.SlurryLiquid was initialized correctly.
I’m not sure why the initialization region isn’t being displayed. I’ll try to find the cause.
Looking at the log you posted, it appears the simulation diverged. Given that the volume fraction was around 1.12195e-5 at the start of the calculation, I suspect the problem might be that the initialization wasn’t performed correctly.
First, I think you should check in Paraview or [Results-Scaffolds-Graphics] to see if the value of alpha.SlurryLiquid was initialized correctly.
I’m not sure why the initialization region isn’t being displayed. I’ll try to find the cause.
Quote from Jake on April 26, 2026, 11:20 pmHi Yashraj,
This is Jake, a software developer for BARAM.
Thank you for bringing this to our attention. We actually haven't encountered this specific issue with the advanced initialization sections before, so I would like to investigate it further.
Could you share your project folder with me? Having your files will allow me to reproduce the environment and trace the bug on my end.
You can send it via [my Dropbox link].
Best,
Jake
Hi Yashraj,
This is Jake, a software developer for BARAM.
Thank you for bringing this to our attention. We actually haven't encountered this specific issue with the advanced initialization sections before, so I would like to investigate it further.
Could you share your project folder with me? Having your files will allow me to reproduce the environment and trace the bug on my end.
You can send it via [my Dropbox link].
Best,
Jake
Quote from Yash R on April 27, 2026, 1:20 pmQuote from Jake on April 26, 2026, 11:20 pmHi Yashraj,
This is Jake, a software developer for BARAM.
Thank you for bringing this to our attention. We actually haven't encountered this specific issue with the advanced initialization sections before, so I would like to investigate it further.
Could you share your project folder with me? Having your files will allow me to reproduce the environment and trace the bug on my end.
You can send it via [my Dropbox link].
Best,
JakeHello Jake,
Thank you for your response. I was trying to upload the files to your dropbox but I wasn't able to upload the files yet as the link says it's for sharing your folder with me and I can't upload mine to it, could you kindly share a "Request file" link and I shall upload the files.Looking forward to your response.
Kind regards,
Yash Randad
Quote from Jake on April 26, 2026, 11:20 pmHi Yashraj,
This is Jake, a software developer for BARAM.
Thank you for bringing this to our attention. We actually haven't encountered this specific issue with the advanced initialization sections before, so I would like to investigate it further.
Could you share your project folder with me? Having your files will allow me to reproduce the environment and trace the bug on my end.
You can send it via [my Dropbox link].
Best,
Jake
Hello Jake,
Thank you for your response. I was trying to upload the files to your dropbox but I wasn't able to upload the files yet as the link says it's for sharing your folder with me and I can't upload mine to it, could you kindly share a "Request file" link and I shall upload the files.
Looking forward to your response.
Kind regards,
Yash Randad
Quote from Yash R on April 27, 2026, 1:27 pmQuote from bykima5230416a7 on April 26, 2026, 2:48 pmLooking at the log you posted, it appears the simulation diverged. Given that the volume fraction was around 1.12195e-5 at the start of the calculation, I suspect the problem might be that the initialization wasn’t performed correctly.
First, I think you should check in Paraview or [Results-Scaffolds-Graphics] to see if the value of alpha.SlurryLiquid was initialized correctly.
I’m not sure why the initialization region isn’t being displayed. I’ll try to find the cause.
Hello Bykima,
Thanks for your response.
I agree that there is some issue with initialisation. I tried what you said and checked on Paraview and, as seen in the attached image, the value for alpha.SlurryLiquid is 0 everywhere even though it should be 1 within the advanced sections created in the initialization tab.
Please do let me know should you need any further information to look into this. I appreciate the help
Kind regards,
Yash Randad
Quote from bykima5230416a7 on April 26, 2026, 2:48 pmLooking at the log you posted, it appears the simulation diverged. Given that the volume fraction was around 1.12195e-5 at the start of the calculation, I suspect the problem might be that the initialization wasn’t performed correctly.
First, I think you should check in Paraview or [Results-Scaffolds-Graphics] to see if the value of alpha.SlurryLiquid was initialized correctly.
I’m not sure why the initialization region isn’t being displayed. I’ll try to find the cause.
Hello Bykima,
Thanks for your response.
I agree that there is some issue with initialisation. I tried what you said and checked on Paraview and, as seen in the attached image, the value for alpha.SlurryLiquid is 0 everywhere even though it should be 1 within the advanced sections created in the initialization tab.
Please do let me know should you need any further information to look into this. I appreciate the help
Kind regards,
Yash Randad
Uploaded files:Quote from Yash R on April 27, 2026, 3:34 pmQuote from Jake on April 27, 2026, 2:19 pmDear Yash,
Sorry for the wrong link.
I've updated the link in my previous post.Kind Regards,
JakeDear Jake,
I have uploaded the project files on your dropbox. Feel free to reach out to me should anything else be needed.
Thanking you,
Yash Randad
Quote from Jake on April 27, 2026, 2:19 pmDear Yash,
Sorry for the wrong link.
I've updated the link in my previous post.Kind Regards,
Jake
Dear Jake,
I have uploaded the project files on your dropbox. Feel free to reach out to me should anything else be needed.
Thanking you,
Yash Randad
Quote from Jake on April 28, 2026, 12:43 pmHi Yash,
I've received the files and checked them.
Actually those initialization sections are there.
They are just too small.
You may need to scale the mesh.
Have a look at the attached files.Regards,
Jake
Hi Yash,
I've received the files and checked them.
Actually those initialization sections are there.
They are just too small.
You may need to scale the mesh.
Have a look at the attached files.
Regards,
Jake
Quote from Yash R on April 29, 2026, 4:35 amQuote from Jake on April 28, 2026, 12:43 pmHi Yash,
I've received the files and checked them.
Actually those initialization sections are there.
They are just too small.
You may need to scale the mesh.
Have a look at the attached files.Regards,
JakeHello Jake,
Thank you for pointing it out. It was a silly error on my end. I have now scaled up the advanced sections from millimetres to metres as it should be, however, even though the initialisation goes as expected (I checked on ParaView) my calculation still terminates/crashes.I really need some additional help with my project, would it be possible to contact you via email?
I would appreciate it loads.Thank you,
Yash Randad
Quote from Jake on April 28, 2026, 12:43 pmHi Yash,
I've received the files and checked them.
Actually those initialization sections are there.
They are just too small.
You may need to scale the mesh.
Have a look at the attached files.Regards,
Jake
Hello Jake,
Thank you for pointing it out. It was a silly error on my end. I have now scaled up the advanced sections from millimetres to metres as it should be, however, even though the initialisation goes as expected (I checked on ParaView) my calculation still terminates/crashes.
I really need some additional help with my project, would it be possible to contact you via email?
I would appreciate it loads.
Thank you,
Yash Randad
Quote from Jake on April 30, 2026, 7:49 pmHello Yash,
I may not be helpful to you since I'm a software developer rather than a CFD engineer.
You can ask help via marketing@nextfoam.co.kr.
My colleagues who are experts in CFD will help you.Regards,
Jake
Hello Yash,
I may not be helpful to you since I'm a software developer rather than a CFD engineer.
You can ask help via marketing@nextfoam.co.kr.
My colleagues who are experts in CFD will help you.
Regards,
Jake







