Simplifies the setting of the scheme for the phase pressure, e.g. choosing localMax
interpolationSchemes
{
default linear;
pPrime localMax;
}
improves stability and reduces chequerboarding in the solution at higher Courant
numbers.
In order that the phase-fractions sum to 1 it is necessary that the same
diffusivity is used for ALL phases in the implicitPhasePressure option. This is
guaranteed by the new alphaDByAf function which returns a single
surfaceScalarField diffusivity to be used when forming the Laplacian term in the
implicit phase-fraction diffusion correction equation in phaseSystemSolve.
The phase-pressure and turbulent dispersion interface terms are summed over all
phases and interfaces in alphaDByAf to form a single diffusivity.
The timeName() function simply returns the dimensionedScalar::name() which holds
the user-time name of the current time and now that timeName() is no longer
virtual the dimensionedScalar::name() can be called directly. The timeName()
function implementation is maintained for backward-compatibility.
Description
Uniform or non-uniform constant solid thermodynamic properties
Each physical property can specified as either \c uniform in which case the
value entry is read, \c zonal in which case the value entry and zone list
are read or \c file in which case the field file in read from the constant
directory.
Usage
Example of uniform constant solid properties specification:
\verbatim
thermoType constSolidThermo;
rho
{
type uniform;
value 8940;
}
Cv
{
type uniform;
value 385;
}
kappa
{
type uniform;
value 380;
}
\endverbatim
Example of zonal constant solid properties specification where kappa is
different in different zones:
\verbatim
thermoType constSolidThermo;
rho
{
type uniform;
value 8940;
}
Cv
{
type uniform;
value 385;
}
kappa
{
type zonal;
value 380;
zones
{
heater 560;
insulation 100;
}
}
\endverbatim
Example of non-uniform constant solid properties specification:
\verbatim
thermoType constSolidThermo;
rho
{
type file;
}
Cv
{
type file;
}
kappa
{
type file;
}
\endverbatim
where each of the field files are read from the constant directory.
A set of routines for cutting polyhedra have been added. These can cut
polyhedral cells based on the adjacent point values and an iso-value
which defines the surface. The method operates directly on the
polyhedral cells; it does not decompose them into tetrahedra at any
point. The routines can compute the cut topology as well as integrals of
properties above and below the cut surface.
An iso-surface algorithm has been added based on these polyhedral
cutting routines. It is significantly more robust than the previous
algorithm, and produces compact surfaces equivalent to the previous
algorithm's maximum filtering level. It is also approximately 3 times
faster than the previous algorithm, and 10 times faster when run
repeatedly on the same set of cells (this is because some addressing is
cached and reused).
This algorithm is used by the 'isoSurface', 'distanceSurface' and
'cutPlane' sampled surfaces.
The 'cutPlane' sampled surface is a renaming of 'cuttingPlane' to make
it consistent with the corresponding packaged function. The name
'cuttingPlane' has been retained for backwards compatibility and can
still be used to select a 'cutPlane' surface. The legacy 'plane' surface
has been removed.
The 'average' keyword has been removed from specification of these
sampled surfaces as cell-centred values are no longer used in the
generation of or interpolation to an iso-surface. The 'filtering'
keyword has also been removed as it relates to options within the
previous algorithm. Zone support has been reinstated into the
'isoSurface' sampled surface. Interpolation to all these sampled
surfaces has been corrected to exactly match the user-selected
interpolation scheme, and the interpolation procedure no longer
unnecessarily re-generates data that is already available.
Now fluxes are updated from the mapped fields following mesh topology change
with or without implicit continuity correction enabled by the optional
correctPhi switch.
Given that the number of solid solver modules is currently 1 and unlikely to
exceed 3 it is not very useful to maintain solid and fluid sub-directories and
easier to see the correspondence between the solver modules and tutorial cases
without.
This adds cavitation modelling to the multiphaseEuler solver module as a
phaseTransfer model. The underlying cavitation modelling is the same as
for the compressibleVoF module.
An example specification in constant/phaseProperties is shown below:
phaseTransfer
{
gas_liquid
{
type cavitation;
model Kunz;
liquid water;
pSat 80000;
UInf 5.33;
tInf 0.028142589;
Cc 100;
Cv 100;
}
}
Based on code contributed by Petteri Peltonen, VTT.
The cavitation models used by the compressibleVoF module can now have a
temperature-dependent saturation pressure model specified. For example,
in the constant/fvModels file of a compressibleVoF case:
VoFCavitation
{
type VoFCavitation;
libs ("libcompressibleVoFCavitation.so");
model SchnerrSauer;
liquid water;
// Constant saturation pressure
//pSat 2300;
// Antoine equation for temperature-dependent saturation pressure
pSat
{
type Antoine;
A 22;
B -3000;
C -500;
}
n 1.6e+13;
dNuc 2.0e-06;
Cc 1;
Cv 1;
}
The cavitation models used by the interFoam solver and the
compressibleVoF solver module can now be applied regardless of the
ordering of the liquid and vapour phases. A "liquid" keyword is now
required in the model specification in order to control which phase is
considered to be the condensed liquid state. Previously the liquid phase
was assumed to be the first of the two phases.
The multiphaseEuler module now uses saturation models from the
centralised thermophysical properties library.
The control of these models is slightly different than for the previous
multiphaseEuler-specific saturation models. Where previously a
"saturationPressure" or "saturationTemperature" sub-dictionary was
employed, now "pSat" and "Tsat" entries are used which can be specified
flexibly in a similar manner to function1-s. See the previous commit for
details.
For high-speed flow cases benefiting from extrapolated pressure, e.g. IC engine
piston motion the fixedFluxExtrapolatedPressure pressure BC can now be used with
the transonic pressure solution option.
Class
Foam::coupledMultiphaseTemperatureFvPatchScalarField
Description
Mixed boundary condition for the phase temperature of a phase in an
Euler-Euler multiphase simulation, to be used for heat-transfer with another
region in a CHT case. Optional thin wall material layer resistances can be
specified through thicknessLayers and kappaLayers entries.
See also
Foam::coupledTemperatureFvPatchScalarField
The new tutorial case tutorials/modules/CHT/multiphaseCoolingCylinder2D is a
variant of the coolingCylinder2D case in which a 10% oil droplets in water
mixture flows over and cools a hot cylinder. The case in run with the
foamMultiRun multi-solver executor.
The thermophysical boundary conditions have be moved from the
multiphaseCompressibleMomentumTransportModels library into the new
multiphaseThermophysicalTransportModels library.
Mass transfer rates are now updated following a change in the pressure
if the mass transfer modelling provides a pressure coefficient. This
means that pimple correctors can be used to improve the behaviour of
mass transfer processes that coupled closely to the pressure field.
Simulating the mixing of two miscible liquids is possible my considering
them as different species of a multicomponent fluid. This approach also
supports an arbitrary number of liquids. The twoLiquidMixingFoam solver
has therefore been removed and its tutorials converted to use the
multicomponentFluid solver module.
The nearest, matching and inverseDistance methods are now based on a
shared "nearby" method. This method creates, for each face, a local
stencil of opposing faces for which the bounding spheres overlap. This
has proven far more robust on cases with both conformal and
non-conformal interfaces.
Bubble waiting time ratio has been made a user adjustable parameter, and
the names of the fields reported by the wallBoilingProperties function
have been rationalised.
Now cases with mesh refinement/unrefinement can be run with the 2nd-order
backward time scheme. However this is for static meshes only, 2nd-order in time
with topology change AND mesh-motion is not currently supported.
This function looks up wall boiling wall functions and collects and
writes out the following data:
- Bubble departure diameter
- Bubble departure frequency
- Nucleation site density
- Effective liquid fraction at the wall
- Quenching heat flux
- Evaporative heat flux
Example of function object specification:
\verbatim
writeWallBoilingProperties
{
type wallBoilingProperties;
functionObjectLibs ( "libmultiphaseEulerFoamFunctionObjects.so" );
writeControl writeTime;
phase liquid;
}
\endverbatim
Patch contributed by Juho Peltola, VTT.
executed with foamRun for single region simulations of foamMultiRun for
multi-region simulations. Replaces multiphaseEulerFoam and all the
corresponding tutorials have been updated and moved to
tutorials/modules/multiphaseEuler.
Class
Foam::solvers::multiphaseEuler
Description
Solver module for a system of any number of compressible fluid phases with a
common pressure, but otherwise separate properties. The type of phase model
is run time selectable and can optionally represent multiple species and
in-phase reactions. The phase system is also run time selectable and can
optionally represent different types of momentum, heat and mass transfer.
Uses the flexible PIMPLE (PISO-SIMPLE) solution for time-resolved and
pseudo-transient and steady simulations.
Optional fvModels and fvConstraints are provided to enhance the simulation
in many ways including adding various sources, Lagrangian
particles, surface film etc. and constraining or limiting the solution.
SourceFiles
multiphaseEuler.C
See also
Foam::solvers::compressibleVoF
Foam::solvers::fluidSolver
Foam::solvers::incompressibleFluid
