- Feb 17, 2017
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Henry Weller authored
The defaultCoeffs entry is now redundant and supported only for backward compatibility. To specify a liquid with default coefficients simply leave the coefficients dictionary empty: liquids { H2O {} } Any or all of the coefficients may be overridden by specifying the properties in the coefficients dictionary, e.g. liquids { H2O { rho { a 1000; b 0; c 0; d 0; } } }
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Henry Weller authored
When liquids are constructed from dictionary the coefficients are now first initialized to their standard values and overridden by the now optional entries provided in the dictionary. For example to specify water with all the standard temperature varying properties but override only the density with a constant value of 1000 specify in thermophysicalProperties liquids { H2O { defaultCoeffs no; H2OCoeffs { rho { a 1000; b 0; c 0; d 0; } } } }
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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
The fundamental properties provided by the specie class hierarchy were mole-based, i.e. provide the properties per mole whereas the fundamental properties provided by the liquidProperties and solidProperties classes are mass-based, i.e. per unit mass. This inconsistency made it impossible to instantiate the thermodynamics packages (rhoThermo, psiThermo) used by the FV transport solvers on liquidProperties. In order to combine VoF with film and/or Lagrangian models it is essential that the physical propertied of the three representations of the liquid are consistent which means that it is necessary to instantiate the thermodynamics packages on liquidProperties. This requires either liquidProperties to be rewritten mole-based or the specie classes to be rewritten mass-based. Given that most of OpenFOAM solvers operate mass-based (solve for mass-fractions and provide mass-fractions to sub-models it is more consistent and efficien...
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- Feb 13, 2017
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Henry Weller authored
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- Feb 12, 2017
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Henry Weller authored
functionObjects::scalarTransport: Added support for optional laminar and turbulent diffusion coefficients Description Evolves a passive scalar transport equation. - To specify the field name set the \c field entry - To employ the same numerical schemes as another field set the \c schemesField entry, - A constant diffusivity may be specified with the \c D entry, - Alternatively if a turbulence model is available a turbulent diffusivity may be constructed from the laminar and turbulent viscosities using the optional diffusivity coefficients \c alphaD and \c alphaDt (which default to 1): \verbatim D = alphaD*nu + alphaDt*nut \endverbatim Resolves feature request https://bugs.openfoam.org/view.php?id=2453
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- Feb 09, 2017
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Henry Weller authored
Resolves bug-report https://bugs.openfoam.org/view.php?id=2455
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Henry Weller authored
Now the interFoam and compressibleInterFoam families of solvers use the same alphaEqn formulation and supporting all of the MULES options without code-duplication. The semi-implicit MULES support allows running with significantly larger time-steps but this does reduce the interface sharpness.
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- Feb 08, 2017
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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
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Henry Weller authored
Description Simple solidification porosity model This is a simple approximation to solidification where the solid phase is represented as a porous blockage with the drag-coefficient evaluated from \f[ S = - \alpha \rho D(T) U \f] where \vartable \alpha | Optional phase-fraction of solidifying phase D(T) | User-defined drag-coefficient as function of temperature \endvartable Note that the latent heat of solidification is not included and the temperature is unchanged by the modelled change of phase. Example of the solidification model specification: \verbatim type solidification; solidificationCoeffs { // Solidify between 330K and 330.5K D table ( (330.0 10000) // Solid below 330K (330.5 0) // Liquid above 330.5K ); // Optional phase-fraction of solidifying phase alpha alpha.liquid; // Solidification porosity is isotropic // use the global coordinate system coordinateSystem { type cartesian; origin (0 0 0); coordinateRotation { type axesRotation; e1 (1 0 0); e2 (0 1 0); } } } \endverbatim
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- Feb 07, 2017
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Henry Weller authored
Description Simple solidification porosity model This is a simple approximation to solidification where the solid phase is represented as a porous blockage with the drag-coefficient evaluated from \f[ S = - \rho D(T) U \f] where \vartable D(T) | User-defined drag-coefficient as function of temperature \endvartable Note that the latent heat of solidification is not included and the temperature is unchanged by the modelled change of phase. Example of the solidification model specification: \verbatim type solidification; solidificationCoeffs { // Solidify between 330K and 330.5K D table ( (330.0 10000) // Solid below 330K (330.5 0) // Liquid above 330.5K ); // Solidification porosity is isotropic // use the global coordinate system coordinateSystem { type cartesian; origin (0 0 0); coordinateRotation { type axesRotation; e1 (1 0 0); e2 (0 1 0); } } } \endverbatim
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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
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- Feb 06, 2017
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Henry Weller authored
Patch contributed by Timo Niemi, VTT. Resolves patch request https://bugs.openfoam.org/view.php?id=2452
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- Feb 03, 2017
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Henry Weller authored
if convergence is not achieved within the maximum number of iterations. Sometimes, particularly running in parallel, PBiCG fails to converge or diverges without warning or obvious cause leaving a solution field containing significant errors which can cause divergence of the application. PBiCGStab is more robust and does not suffer from the problems encountered with PBiCG.
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Henry Weller authored
Compressing and decompressing binary files introduces a significant IO overhead without a providing significant reduction in file-size.
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Henry Weller authored
Patch contributed by Mattijs Janssens
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Henry Weller authored
Patch contributed by Mattijs Janssens
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Henry Weller authored
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Henry Weller authored
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Henry Weller authored
kOmegaSSTSato: Change correctNut() to correctNut(S2, F2) Resolves bug-report https://bugs.openfoam.org/view.php?id=2450
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- Feb 02, 2017
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Henry Weller authored
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- Jan 30, 2017
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Henry Weller authored
Patch contributed by Juho Peltola, VTT Resolves patch request https://bugs.openfoam.org/view.php?id=2446
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Henry Weller authored
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Henry Weller authored
Patch contributed by Juho Peltola, VTT. Resolves patch request https://bugs.openfoam.org/view.php?id=2443
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- Jan 28, 2017
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Henry Weller authored
Patch contributed by Bruno Santos Resolves bug-report https://bugs.openfoam.org/view.php?id=2441
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Henry Weller authored
Patch contributed by Bruno Santos Resolves patch request https://bugs.openfoam.org/view.php?id=2444
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Henry Weller authored
Patch contributed by Bruno Santos Resolves patch request https://bugs.openfoam.org/view.php?id=2424
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- Jan 26, 2017
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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
Patch contributed by Timo Niemi, VTT. Resolves bug-report https://bugs.openfoam.org/view.php?id=2442
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- Jan 25, 2017
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Henry Weller authored
The previous time-step compression flux is not valid/accurate on the new mesh and it is better to re-calculate it rather than map it from the previous mesh to the new mesh.
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