- Jul 19, 2015
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Henry Weller authored
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- Jul 17, 2015
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Henry Weller authored
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Henry Weller authored
Also removed __GNUC__ conditional compilation statements which are no longer needed.
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- Jul 16, 2015
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Henry Weller authored
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Henry Weller authored
The interfacial temperature is assumed equal to the saturation temperature. Only a single species is considered volatile and the other species to not affect the mass-transfer.
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Henry Weller authored
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- Jul 15, 2015
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Henry Weller authored
Added calls to setFluxRequired for p, p_rgh etc. in all solvers which avoids the need to add fluxRequired entries in fvSchemes dictionaries.
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Henry Weller authored
Added calls to setFluxRequired for p in all incompressible solvers which avoids the need to add fluxRequired entries in fvSchemes dictionary. Will add calls to setFluxRequired to the rest of the solvers.
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Henry Weller authored
Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1787
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- Jul 04, 2015
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Henry Weller authored
Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1773
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Henry Weller authored
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Henry Weller authored
Currently this is implemented only for the Antoine equation, for the other more complex models an iterative inversion from pressure to temperature is required.
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- Jul 03, 2015
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Henry Weller authored
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Henry Weller authored
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Henry Weller authored
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Henry Weller authored
In preparation for adding the Tsat function
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Henry Weller authored
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Henry Weller authored
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Henry Weller authored
for consistency with the evaluation of the interface temperature.
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- Jul 02, 2015
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Henry Weller authored
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Henry Weller authored
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- Jul 01, 2015
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Henry Weller authored
Generally this term has a VERY small effect on temperature, it is only important for low-speed buoyancy-dominated flows. Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1755 See also http://cfd.direct/openfoam/energy-equation/
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- Jun 30, 2015
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Henry Weller authored
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Henry Weller authored
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Henry Weller authored
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- Jun 29, 2015
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Henry Weller authored
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- Jun 28, 2015
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Henry Weller authored
Now the specification of the LTS time scheme is simply: ddtSchemes { default localEuler; }
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Henry Weller authored
Replaces LTSReactingParcelFoam and LTSCoalChemistryFoam Select LTS via the ddtScheme: ddtSchemes { default localEuler rDeltaT; }
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- Jun 27, 2015
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Henry Weller authored
Select LTS via the ddtScheme: ddtSchemes { default localEuler rDeltaT; }
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Henry Weller authored
Select LTS via the ddtScheme: ddtSchemes { default localEuler rDeltaT; }
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Henry Weller authored
Select LTS via the ddtScheme: ddtSchemes { default localEuler rDeltaT; }
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Henry Weller authored
Select using the optional consistent true; setting in the PIMPLE dictionary of fvSolution. This option is generally only beneficial for cases run in PIMPLE-mode with a large maximum Courant number.
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Henry Weller authored
See tutorials/compressible/rhoSimpleFoam/squareBend SIMPLE { nNonOrthogonalCorrectors 0; rhoMin 0.1; rhoMax 1.0; transonic yes; consistent yes; residualControl { p 1e-3; U 1e-4; e 1e-3; // possibly check turbulence fields "(k|epsilon|omega)" 1e-3; } } relaxationFactors { fields { p 1; rho 1; } equations { p 1; U 0.9; e 0.9; k 0.9; epsilon 0.9; } }
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Henry Weller authored
e.g. in tutorials/compressible/rhoPimpleFoam/ras/angledDuctLTS PIMPLE { momentumPredictor yes; transonic no; nOuterCorrectors 50; nCorrectors 1; nNonOrthogonalCorrectors 0; consistent yes; rhoMin 0.5; rhoMax 2.0; residualControl { "(U|k|epsilon)" { relTol 0; tolerance 0.0001; } } turbOnFinalIterOnly off; } relaxationFactors { fields { "p.*" 0.9; "rho.*" 1; } equations { "U.*" 0.9; "h.*" 0.7; "(k|epsilon|omega).*" 0.8; } }
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Henry Weller authored
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Henry Weller authored
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Henry Weller authored
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- Jun 26, 2015
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Henry Weller authored
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Henry Weller authored
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