- Dec 01, 2017
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Patch contributed by Mattijs Janssens Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1692
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- May 14, 2018
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Andrew Heather authored
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- Dec 14, 2017
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Thermo and reaction thermo macros have been renamed and refactored. If the name is plural (make???Thermos) then it adds the model to all selection tables. If not (make???Thermo) then it only adds to the requested psi or rho table.
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- Dec 01, 2017
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This mixture allows a reacting solver to be used with a single component fluid without the additional case files usually required for reacting thermodynamics. reactionThermo: Instantiated more single component mixtures ENH: reactionThermo: Select singleComponentMixture as pureMixture A pureMixture can now be specified in a reacting solver. This further enhances compatibility between non-reacting and reacting solvers. To achieve this, mixtures now have a typeName function of the same form as the lower thermodyanmic models. In addition, to avoid name clashes, the reacting thermo make macros have been split into those that create entries on multiple selection tables, and those that just add to the reaction thermo table.
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- Nov 23, 2017
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The combustion and chemistry models no longer select and own the thermodynamic model; they hold a reference instead. The construction of the combustion and chemistry models has been changed to require a reference to the thermodyanmics, rather than the mesh and a phase name. At the solver-level the thermo, turbulence and combustion models are now selected in sequence. The cyclic dependency between the three models has been resolved, and the raw-pointer based post-construction step for the combustion model has been removed. The old solver-level construction sequence (typically in createFields.H) was as follows: autoPtr<combustionModels::psiCombustionModel> combustion ( combustionModels::psiCombustionModel::New(mesh) ); psiReactionThermo& thermo = combustion->thermo(); // Create rho, U, phi, etc... autoPtr<compressible::turbulenceModel> turbulence ( compressible::turbulenceModel::New(rho, U, phi, thermo) ); combustion->setTurbulence(*turbulence); The new sequence is: autoPtr<psiReactionThermo> thermo(psiReactionThermo::New(mesh)); // Create rho, U, phi, etc... autoPtr<compressible::turbulenceModel> turbulence ( compressible::turbulenceModel::New(rho, U, phi, *thermo) ); autoPtr<combustionModels::psiCombustionModel> combustion ( combustionModels::psiCombustionModel::New(*thermo, *turbulence) ); ENH: combustionModel, chemistryModel: Simplified model selection The combustion and chemistry model selection has been simplified so that the user does not have to specify the form of the thermodynamics. Examples of new combustion and chemistry entries are as follows: In constant/combustionProperties: combustionModel PaSR; combustionModel FSD; In constant/chemistryProperties: chemistryType { solver ode; method TDAC; } All the angle bracket parts of the model names (e.g., <psiThermoCombustion,gasHThermoPhysics>) have been removed as well as the chemistryThermo entry. The changes are mostly backward compatible. Only support for the angle bracket form of chemistry solver names has been removed. Warnings will print if some of the old entries are used, as the parts relating to thermodynamics are now ignored. ENH: combustionModel, chemistryModel: Simplified model selection Updated all tutorials to the new format STYLE: combustionModel: Namespace changes Wrapped combustion model make macros in the Foam namespace and removed combustion model namespace from the base classes. This fixes a namespace specialisation bug in gcc 4.8. It is also somewhat less verbose in the solvers. This resolves bug report https://bugs.openfoam.org/view.php?id=2787 ENH: combustionModels: Default to the "none" model When the constant/combustionProperties dictionary is missing, the solver will now default to the "none" model. This is consistent with how radiation models are selected.
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- Dec 01, 2017
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ENH: multiphaseInterFoam: Merged dynamic mesh functionality of multiphaseInterDyMFoam into multiphaseInterFoam and replaced multiphaseInterDyMFoam with a script which reports this change. The multiphaseInterDyMFoam tutorials have been moved into the multiphaseInterFoam directory. This change is one of a set of developments to merge dynamic mesh functionality into the standard solvers to improve consistency, usability, flexibility and maintainability of these solvers. Henry G. Weller CFD Direct Ltd.
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- Nov 30, 2017
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and replaced interDyMFoam with a script which reports this change. The interDyMFoam tutorials have been moved into the interFoam directory. This change is one of a set of developments to merge dynamic mesh functionality into the standard solvers to improve consistency, usability, flexibility and maintainability of these solvers. Henry G. Weller CFD Direct Ltd. interMixingFoam, multiphaseInterFoam: Updated for changes to interFoam
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Added support for mesh-motion update within PIMPLE loop in pimpleFoam and rhoPimpleFoam.
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- May 11, 2018
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Andrew Heather authored
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- Nov 23, 2017
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and replaced rhoPimpleDyMFoam with a script which reports this change. The rhoPimpleDyMFoam tutorials have been moved into the rhoPimpleFoam directory. This change is the first of a set of developments to merge dynamic mesh functionality into the standard solvers to improve consistency, usability, flexibility and maintainability of these solvers. Henry G. Weller CFD Direct Ltd. rhoReactingFoam: Updated for changes to rhoPimpleFoam files
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- Nov 18, 2017
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Now pimpleDyMFoam is exactly equivalent to pimpleFoam when running on a staticFvMesh. Also when the constant/dynamicMeshDict is not present a staticFvMesh is automatically constructed so that the pimpleDyMFoam solver can run any pimpleFoam case without change. pimpleDyMFoam: Store Uf as an autoPtr for better error handling pimpleFoam: Set initial deltaT from the Courant number for improved stability on start-up and compatibility with pimpleDyMFoam ENH: pimpleFoam: Merged dynamic mesh functionality of pimpleDyMFoam into pimpleFoam and replaced pimpleDyMFoam with a script which reports this change. The pimpleDyMFoam tutorials have been moved into the pimpleFoam directory. This change is the first of a set of developments to merge dynamic mesh functionality into the standard solvers to improve consistency, usability, flexibility and maintainability of these solvers. Henry G. Weller CFD Direct Ltd. tutorials/incomp...
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- Aug 18, 2017
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- Oct 10, 2017
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- May 10, 2018
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Andrew Heather authored
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- Sep 19, 2017
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XiEngineFoam is a premixed/partially-premixed combustion engine solver which exclusively uses the Xi flamelet combustion model. engineFoam is a general engine solver for inhomogeneous combustion with or without spray supporting run-time selection of the chemistry-based combustion model.
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Standard crank-connecting rod and the new free-piston kinematics motion options are provides, others can easily be added. Contributed by Francesco Contino and Nicolas Bourgeois, BURN Research Group.
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- Oct 31, 2017
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The patch magSf calculation has been changed so that it uses the same triangulation as the overlap algorithm. This improves consistency and means that for exactly conforming patches (typically before any mesh motion) the weights do not require normalisation.
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- Dec 09, 2017
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Resolves bug-report https://bugs.openfoam.org/view.php?id=2785 ENH: compressibleInterFoam family: merged two-phase momentum stress modelling from compressibleInterPhaseTransportFoam The new momentum stress model selector class compressibleInterPhaseTransportModel is now used to select between the options: Description Transport model selection class for the compressibleInterFoam family of solvers. By default the standard mixture transport modelling approach is used in which a single momentum stress model (laminar, non-Newtonian, LES or RAS) is constructed for the mixture. However if the \c simulationType in constant/turbulenceProperties is set to \c twoPhaseTransport the alternative Euler-Euler two-phase transport modelling approach is used in which separate stress models (laminar, non-Newtonian, LES or RAS) are instantiated for each of the two phases allowing for different modeling for the phases. Mixture and two-phase momentum stress modelling is now supported in compressibleInterFoam, compressibleInterDyMFoam and compressibleInterFilmFoam. The prototype compressibleInterPhaseTransportFoam solver is no longer needed and has been removed.
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- Nov 10, 2017
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Patch contributed by Mattijs Janssens Resolves bug-report https://bugs.openfoam.org/view.php?id=2744
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- Nov 07, 2017
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Another exception has been added to globalIndexAndTransform to prevent transformations being generated from coupled patch pairs marked with coincident-full-match transformations. Foamy generates such patches, and the faces on them at intermediate stages of meshing can be degenerate, making the calculation of transformations unreliable. This change enforces the definition that coincident-full-match patch pairs are not transformed.
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- Oct 27, 2017
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Patch contributed by Mattijs Janssens Resolves bug-report https://bugs.openfoam.org/view.php?id=2712
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- Oct 23, 2017
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To unsure fvOptions are instantiated for post-processing createFvOptions.H must be included in createFields.H rather than in the solver directly. Resolves bug-report https://bugs.openfoam.org/view.php?id=2733 BUG: porousSimpleFoam: moved createFvOptions.H into createFields.H for -postProcess option Resolves bug-report https://bugs.openfoam.org/view.php?id=2733 BUG: solvers: Moved fvOption construction into createFields.H for post-processing This ensures that the fvOptions are constructed for the -postProcessing option so that functionObjects which process fvOption data operate correctly in this mode.
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- Oct 19, 2017
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by setting the optional switch YInfZero to true.
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- Oct 18, 2017
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in the limit of the phase fraction -> 0 Can be used with the Maxwell non-Newtonian laminar stress model when used in multiphase solvers.
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- Sep 04, 2017
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Patch contributed by Bruno Santos Resolves patch request https://bugs.openfoam.org/view.php?id=2684
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- Apr 04, 2018
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Andrew Heather authored
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- Jul 13, 2017
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for consistency with other rotating BCs.
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- Dec 14, 2017
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- Dec 15, 2017
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e.g. odeCoeffs { solver seulex; absTol 1e-12; relTol 0.0001; maxSteps 1e+06; } maxSteps defaults to 10000 for backward compatibility.
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- Dec 13, 2017
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The absolute value of the the time has been added to the rigid body model state. This value is not directly necessary for calculating the evolution of the rigid body system, it just facilitates the implementation of sub-models which are in some way time-dependent.
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- Dec 01, 2017
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Mixture molecular weight is now evaluated in heThermo like everything else, relying on the low level specie mixing rules. Units have also been corrected. SpecieMixture: Pure virtual definition for W to prevent Clang warning
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- Nov 29, 2017
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- Nov 22, 2017
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- Nov 16, 2017
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to support the evaporation of the solvent from the wax film and the changes in viscosity caused by the reduction in solvent content. BUG: filmViscosityModel::thixotropicViscosity: Corrected sign of impingement rate to compensate for rhoSp having the wrong sign BUG: surfaceFilmModels::waxSolventEvaporation: Corrected handling of impingement ENH: surfaceFilmModels::waxSolventViscosity: Changed mixing to mole-fraction based ENH: surfaceFilmModels::thermoSingleLayer: Added call to solveContinuity before updateSubmodels to allow sub-models to solve transport equations for conserved properties
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- Nov 14, 2017
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Resolves bug-report https://bugs.openfoam.org/view.php?id=2758
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