Commit Graph

8 Commits

Author SHA1 Message Date
e352828514 reactingMultiphaseEulerFoam: Stationary phase
Two new phase models have been added as selectable options for
reactingMultiphaseEulerFoam; pureStationaryPhaseModel and
pureStationaryIsothermalPhaseModel. These phases do not store a
velocity and their phase fractions remain constant throughout the
simulation. They are intended for use in modelling static particle beds
and other forms of porous media by means of the existing Euler-Euler
transfer models (drag, heat transfer, etc...).

Note that this functionality has not been extended to
reactingTwoPhaseEulerFoam, or the non-reacting *EulerFoam solvers.

Additional maintenance work has been carried out on the phase model
and phase system structure. The system can now loop over subsets of
phases with specific functionality (moving, multi-component, etc...) in
order to avoid testing for the existence of equations or variables in
the top level solver. The mass transfer handling and it's effect on
per-phase source terms has been refactored to reduce duplication. Const
and non-const access to phase properties has been formalised by renaming
non-const accessors with a "Ref" suffix, which is consistent with other
recent developments to classes including tmp and GeometricField, among
others. More sub-modelling details have been made private in order to
reduce the size of interfaces and improve abstraction.

This work was supported by Zhen Li, at Evonik
2018-03-23 09:08:52 +00:00
0ea0b7c407 combustionModels: Changed the construction order
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)
    );
2017-11-24 22:52:18 +00:00
1a2c77abfa Rationalized heat release rate functions
Combined 'dQ()' and 'Sh()' into 'Qdot()' which returns the heat-release rate in
the normal units [kg/m/s3] and used as the heat release rate source term in
the energy equations, to set the field 'Qdot' in several combustion solvers
and for the evaluation of the local time-step when running LTS.
2016-12-15 17:10:21 +00:00
335df22c82 reactingEulerFoam: Updated to support zoneCombustion models 2016-12-01 15:16:19 +00:00
99c000fc94 Rationalized the indentation of C-preprocessor directives 2016-02-29 15:42:03 +00:00
cc5f67a0ff reactingMultiphaseEulerFoam: New Euler-Euler multiphase solver
Supporting any number of phases with heat and mass transfer, phase-change and reactions
2015-09-11 15:33:12 +01:00
5f8b7eb999 reactingEulerFoam: Correct handling of phaseName in ReactingPhaseModel 2015-08-29 00:02:15 +01:00
f688a0660d reactingTwoPhaseEulerFoam: Moved into reactingEulerFoam
and two-phase functionality separated from multiphase functionality
2015-08-26 12:49:26 +01:00