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Commit 84e3fb4d authored by andy's avatar andy
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ENH: Tutorial update

parent 33496016
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tutorials/lagrangian/LTSReactingParcelFoam/counterFlowFlame2D/0/T
+ 0
− 1
View file @ 84e3fb4d
......@@ -36,7 +36,6 @@ boundaryField
type inletOutlet;
inletValue uniform 293;
value uniform 293;
}
frontAndBack
{
......
tutorials/lagrangian/LTSReactingParcelFoam/counterFlowFlame2D/0/U
+ 2
− 1
View file @ 84e3fb4d
......@@ -33,7 +33,8 @@ boundaryField
}
outlet
{
type zeroGradient;
type pressureInletOutletVelocity;
value $internalField;
}
frontAndBack
{
......
tutorials/lagrangian/LTSReactingParcelFoam/counterFlowFlame2D/0/epsilon deleted 100644 → 0
+ 0
− 45
View file @ 33496016
/*--------------------------------*- C++ -*----------------------------------*\
| ========= | |
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
| \\ / O peration | Version: dev |
| \\ / A nd | Web: www.OpenFOAM.org |
| \\/ M anipulation | |
\*---------------------------------------------------------------------------*/
FoamFile
{
version 2.0;
format ascii;
class volScalarField;
location "0";
object epsilon;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
dimensions [0 2 -3 0 0 0 0];
internalField uniform 50;
boundaryField
{
fuel
{
type fixedValue;
value uniform 1e-05;
}
air
{
type fixedValue;
value uniform 1e-05;
}
outlet
{
type zeroGradient;
}
frontAndBack
{
type empty;
}
}
// ************************************************************************* //
tutorials/lagrangian/LTSReactingParcelFoam/counterFlowFlame2D/0/k deleted 100644 → 0
+ 0
− 45
View file @ 33496016
/*--------------------------------*- C++ -*----------------------------------*\
| ========= | |
| \\ / F ield | OpenFOAM: The Open Source CFD Toolbox |
| \\ / O peration | Version: dev |
| \\ / A nd | Web: www.OpenFOAM.org |
| \\/ M anipulation | |
\*---------------------------------------------------------------------------*/
FoamFile
{
version 2.0;
format ascii;
class volScalarField;
location "0";
object k;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
dimensions [0 2 -2 0 0 0 0];
internalField uniform 3.75e-05;
boundaryField
{
fuel
{
type fixedValue;
value uniform 3.75e-05;
}
air
{
type fixedValue;
value uniform 3.75e-05;
}
outlet
{
type zeroGradient;
}
frontAndBack
{
type empty;
}
}
// ************************************************************************* //
tutorials/lagrangian/LTSReactingParcelFoam/counterFlowFlame2D/0/p
+ 8
− 6
View file @ 84e3fb4d
......@@ -29,14 +29,16 @@ boundaryField
{
type zeroGradient;
}
inlet2
{
type zeroGradient;
}
outlet
{
type fixedValue;
value uniform 1e5;
type totalPressure;
p0 $internalField;
U U;
phi phi;
rho none;
psi none;
gamma 1;
value $internalField;
}
frontAndBack
{
......
tutorials/lagrangian/LTSReactingParcelFoam/counterFlowFlame2D/constant/chemistryProperties
+ 15
− 4
View file @ 84e3fb4d
......@@ -17,14 +17,25 @@ FoamFile
chemistryType
{
chemistrySolver noChemistrySolver;
chemistrySolver EulerImplicit;
chemistryThermo rho;
}
chemistry on; // off;
chemistry on;
chemCalcFreq 1;
initialChemicalTimeStep 1e-07;
initialChemicalTimeStep 1e-8; // NOT USED
EulerImplicitCoeffs
{
cTauChem 1;
equilibriumRateLimiter off;
}
odeCoeffs
{
solver Rosenbrock43;
absTol 1e-12;
relTol 0.01;
}
// ************************************************************************* //
tutorials/lagrangian/LTSReactingParcelFoam/counterFlowFlame2D/constant/combustionProperties
+ 2
− 5
View file @ 84e3fb4d
......@@ -15,15 +15,12 @@ FoamFile
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
combustionModel PaSR<rhoChemistryCombustion>;
combustionModel laminar<rhoChemistryCombustion>;
active true;
PaSRCoeffs
laminarCoeffs
{
Cmix 0.1;
turbulentReaction off;
useReactionRate true;
}
......
tutorials/lagrangian/LTSReactingParcelFoam/counterFlowFlame2D/0/alphat → tutorials/lagrangian/LTSReactingParcelFoam/counterFlowFlame2D/constant/polyMesh/boundary
+ 18
− 16
View file @ 84e3fb4d
......@@ -9,37 +9,39 @@ FoamFile
{
version 2.0;
format ascii;
class volScalarField;
location "0";
object alphat;
class polyBoundaryMesh;
location "constant/polyMesh";
object boundary;
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
dimensions [1 -1 -1 0 0 0 0];
internalField uniform 0;
boundaryField
{
4
(
fuel
{
type fixedValue;
value uniform 0;
type patch;
nFaces 40;
startFace 7860;
}
air
{
type fixedValue;
value uniform 0;
type patch;
nFaces 40;
startFace 7900;
}
outlet
{
type zeroGradient;
type patch;
nFaces 200;
startFace 7940;
}
frontAndBack
{
type empty;
inGroups 1(empty);
nFaces 8000;
startFace 8140;
}
}
)
// ************************************************************************* //
tutorials/lagrangian/LTSReactingParcelFoam/counterFlowFlame2D/constant/turbulenceProperties
+ 1
− 1
View file @ 84e3fb4d
......@@ -15,7 +15,7 @@ FoamFile
}
// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
simulationType RASModel;
simulationType laminar;
// ************************************************************************* //
tutorials/lagrangian/LTSReactingParcelFoam/counterFlowFlame2D/system/controlDict
+ 1
− 1
View file @ 84e3fb4d
......@@ -23,7 +23,7 @@ startTime 0;
stopAt endTime;
endTime 10000;
endTime 2000;
deltaT 1;
......
tutorials/lagrangian/LTSReactingParcelFoam/counterFlowFlame2D/system/fvSolution
+ 40
− 50
View file @ 84e3fb4d
......@@ -17,79 +17,69 @@ FoamFile
solvers
{
rho
"rho.*"
{
solver PCG;
preconditioner DIC;
tolerance 0;
relTol 0.1;
}
rhoFinal
{
solver PCG;
preconditioner DIC;
tolerance 1e-4;
relTol 0;
solver diagonal;
}
p
{
solver GAMG;
tolerance 0;
relTol 0.05;
smoother DICGaussSeidel;
nPreSweeps 0;
nPostSweeps 2;
cacheAgglomeration true;
nCellsInCoarsestLevel 10;
agglomerator faceAreaPair;
mergeLevels 1;
maxIter 50;
};
solver PCG;
preconditioner DIC;
tolerance 1e-6;
relTol 0.1;
}
pFinal
{
$p;
tolerance 1e-4;
relTol 0;
};
}
"(U|Yi|h|k|epsilon)"
"(U|h|k|epsilon)"
{
solver smoothSolver;
smoother GaussSeidel;
tolerance 0;
solver PBiCG;
preconditioner DILU;
tolerance 1e-6;
relTol 0.1;
}
"(U|Yi|h|k|epsilon)Final"
"(U|h|k|epsilon)Final"
{
solver smoothSolver;
smoother GaussSeidel;
tolerance 1e-4;
relTol 0;
$U;
relTol 0.1;
}
Yi
{
$U;
relTol 0.1;
}
}
PIMPLE
{
nCorrectors 2;
momentumPredictor no;
nOuterCorrectors 1;
nCorrectors 1;
nNonOrthogonalCorrectors 0;
momentumPredictor yes;
rhoMin 0.1;
rhoMax 1.5;
maxCo 0.1;
rDeltaTSmoothingCoeff 0.1;
maxDeltaT 2e-4;
alphaTemp 0.005;
maxDeltaT 1e-2;
maxCo 1;
alphaTemp 0.05;
rDeltaTSmoothingCoeff 1;
rDeltaTDampingCoeff 1;
}
relaxationFactors
{
fields
{
}
equations
{
".*" 1;
}
}
......
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