The injection models do not inject parcels into the film they specifically eject
parcels from the film and the name "injection" is very confusing and misleading
hence the logical rename injection -> ejection.
cpp is no longer used to pre-process Make/files files allowing standard make '#'
syntax for comments, 'ifdef', 'ifndef' conditionals etc. This is make possible
by automatically pre-pending SOURCE += to each of the source file names in
Make/files.
The list of source files compile can be specified either as a simple list of
files in Make/files e.g.
# Note: fileMonitor assumes inotify by default. Compile with -DFOAM_USE_STAT
# to use stat (=timestamps) instead of inotify
fileMonitor.C
ifdef SunOS64
dummyPrintStack.C
else
printStack.C
endif
LIB = $(FOAM_LIBBIN)/libOSspecific
or
or directly as the SOURCE entry which is used in the Makefile:
SOURCE = \
adjointOutletPressure/adjointOutletPressureFvPatchScalarField.C \
adjointOutletVelocity/adjointOutletVelocityFvPatchVectorField.C \
adjointShapeOptimizationFoam.C
EXE = $(FOAM_APPBIN)/adjointShapeOptimizationFoam
In either form make syntax for comments and conditionals is supported.
It is better to not select and instantiate a model, fvOption etc. than to create
it and set it inactive as the creation process requires reading of settings,
parameters, fields etc. with all the associated specification and storage
without being used. Also the incomplete implementation added a lot of
complexity in the low-level operation of models introducing a significant
maintenance overhead and development overhead for new models.
The convoluted separate ".*Coeffs" dictionary form of model coefficient
specification is now deprecated and replaced with the simpler sub-dictionary
form but support is provided for the deprecated form for backward comparability.
e.g.
thermophysicalProperties
{
type liquid;
useReferenceValues no;
liquid H2O;
}
rather than
filmThermoModel liquid;
liquidCoeffs
{
useReferenceValues no;
liquid H2O;
}
and
forces
{
thermocapillary;
distributionContactAngle
{
Ccf 0.085;
distribution
{
type normal;
normalDistribution
{
minValue 50;
maxValue 100;
expectation 75;
variance 100;
}
}
zeroForcePatches ();
}
}
rather than
forces
(
thermocapillary
distributionContactAngle
);
distributionContactAngleCoeffs
{
Ccf 0.085;
distribution
{
type normal;
normalDistribution
{
minValue 50;
maxValue 100;
expectation 75;
variance 100;
}
}
zeroForcePatches ();
}
All the tutorial cases containing a surface film have been updated for guidance,
e.g. tutorials/lagrangian/buoyantReactingParticleFoam/hotBoxes/constant/surfaceFilmProperties
surfaceFilmModel thermoSingleLayer;
regionName wallFilmRegion;
active true;
thermophysicalProperties
{
type liquid;
useReferenceValues no;
liquid H2O;
}
viscosity
{
model liquid;
}
deltaWet 1e-4;
hydrophilic no;
momentumTransport
{
model laminar;
Cf 0.005;
}
forces
{
thermocapillary;
distributionContactAngle
{
Ccf 0.085;
distribution
{
type normal;
normalDistribution
{
minValue 50;
maxValue 100;
expectation 75;
variance 100;
}
}
zeroForcePatches ();
}
}
injection
{
curvatureSeparation
{
definedPatchRadii
(
("(cube[0-9][0-9]_side[0-9]_to_cube[0-9][0-9]_side[0-9])" 0)
);
}
drippingInjection
{
cloudName reactingCloud1;
deltaStable 0;
particlesPerParcel 100.0;
parcelDistribution
{
type RosinRammler;
RosinRammlerDistribution
{
minValue 5e-04;
maxValue 0.0012;
d 7.5e-05;
n 0.5;
}
}
}
}
phaseChange
{
model standardPhaseChange;
Tb 373;
deltaMin 1e-8;
L 1.0;
}
upperSurfaceModels
{
heatTransfer
{
model mappedConvectiveHeatTransfer;
}
}
lowerSurfaceModels
{
heatTransfer
{
model constant;
c0 50;
}
}
to provide the same numerical stability control as the other injection models:
BrunDrippingInjection, drippingInjection
//- Stable film thickness - drips only formed if thickness
// exceeds this threshold value
scalar deltaStable_;
Resolves bug-report https://bugs.openfoam.org/view.php?id=2456
providing the shear-stress term in the momentum equation for incompressible and
compressible Newtonian, non-Newtonian and visco-elastic laminar flow as well as
Reynolds averaged and large-eddy simulation of turbulent flow.
The general deviatoric shear-stress term provided by the MomentumTransportModels
library is named divDevTau for compressible flow and divDevSigma (sigma =
tau/rho) for incompressible flow, the spherical part of the shear-stress is
assumed to be either included in the pressure or handled separately. The
corresponding stress function sigma is also provided which in the case of
Reynolds stress closure returns the effective Reynolds stress (including the
laminar contribution) or for other Reynolds averaged or large-eddy turbulence
closures returns the modelled Reynolds stress or sub-grid stress respectively.
For visco-elastic flow the sigma function returns the effective total stress
including the visco-elastic and Newtonian contributions.
For thermal flow the heat-flux generated by thermal diffusion is now handled by
the separate ThermophysicalTransportModels library allowing independent run-time
selection of the heat-flux model.
During the development of the MomentumTransportModels library significant effort
has been put into rationalising the components and supporting libraries,
removing redundant code, updating names to provide a more logical, consistent
and extensible interface and aid further development and maintenance. All
solvers and tutorials have been updated correspondingly and backward
compatibility of the input dictionaries provided.
Henry G. Weller
CFD Direct Ltd.
This provides an extensible and run-time selectable framework to support complex
energy and specie transport models, in particular multi-component diffusion.
Currently only the Fourier for laminar and eddyDiffusivity for RAS and LES
turbulent flows are provided but the interface is general and the set of models
will be expanded in the near future.
Following the generalisation of the TurbulenceModels library to support
non-Newtonian laminar flow including visco-elasticity and extensible to other
form of non-Newtonian behaviour the name TurbulenceModels is misleading and does
not properly represent how general the OpenFOAM solvers now are. The
TurbulenceModels now provides an interface to momentum transport modelling in
general and the plan is to rename it MomentumTransportModels and in preparation
for this the turbulenceProperties dictionary has been renamed momentumTransport
to properly reflect its new more general purpose.
The old turbulenceProperties name is supported for backward-compatibility.
There is now an optional tauy entry in the thixotropicCoeffs to specify the
Bingham yield stress, e.g.:
filmViscosityModel thixotropic;
thixotropicCoeffs
{
mu0 100;
muInf 0.1;
a 0.1;
b 3;
c 0.005;
d 0.9;
tauy 1.1; // Yield stress in Pa
}
to avoid staggering patterns created by an unstable coupling between this term
and the film thickness. Further relaxation of this term may be required for
cases dominated by surface tension effects.
All of the film transport equations are now formulated with respect to the film
volume fraction in the region cell layer rather than the film thickness which
ensures mass conservation of the film even as it flows over curved surfaces and
around corners. (In the previous formulation the conservation error could be as
large as 15% for a film flowing around a corner.)
The film Courant number is now formulated in terms of the film cell volumetric
flux which avoids the stabilised division by the film thickness and provides a
more reliable estimate for time-step evaluation. As a consequence the film
solution is substantially more robust even though the time-step is now
significantly higher. For film flow dominated problem the simulations now runs
10-30x faster.
The inconsistent extended PISO controls have been replaced by the standard
PIMPLE control system used in all other flow solvers, providing consistent
input, a flexible structure and easier maintenance.
The momentum corrector has been re-formulated to be consistent with the momentum
predictor so the optional PIMPLE outer-corrector loop converges which it did not
previously.
nonuniformTransformCyclic patches and corresponding fields are no longer needed
and have been removed which paves the way for a future rationalisation of the
handling of cyclic transformations in OpenFOAM to improve robustness, usability
and maintainability.
Film sources have been simplified to avoid the need for fictitious boundary
conditions, in particular mappedFixedPushedInternalValueFvPatchField which has
been removed.
Film variables previously appended with an "f" for "film" rather than "face"
have been renamed without the unnecessary and confusing "f" as they are
localised to the film region and hence already directly associated with it.
All film tutorials have been updated to test and demonstrate the developments
and improvements listed above.
Henry G. Weller
CFD Direct Ltd.
The pressure provided to the patch and cellSet property evaluation functions is
always that stored by the thermodynamics package as is the composition which is
provided internally; given that these functions are used in boundary conditions
to estimate changes in heat flux corresponding to changes in temperature only
there is no need for another pressure to be provided. In order that the
pressure and composition treatment are consistent and to maintain that during
future rationalisation of the handling of composition it makes sense to remove
this unnecessary pressure argument.
Function1 has been generalised in order to provide functionality
previously provided by some near-duplicate pieces of code.
The interpolationTable and tableReader classes have been removed and
their usage cases replaced by Function1. The interfaces to Function1,
Table and TableFile has been improved for the purpose of using it
internally; i.e., without user input.
Some boundary conditions, fvOptions and function objects which
previously used interpolationTable or other low-level interpolation
classes directly have been changed to use Function1 instead. These
changes may not be backwards compatible. See header documentation for
details.
In addition, the timeVaryingUniformFixedValue boundary condition has
been removed as its functionality is duplicated entirely by
uniformFixedValuePointPatchField.
and removed the need for the direct dependency of Ostream on keyType which is
not a primitive IO type and relates specifically to dictionary and not all IO.
solidChemistryModel is not implemented in a general way but specialised to form
the basis of the highly specific pyrolysis mode. The handling of reactions is
hard-coded for forward reactions only, the Jacobian was present but incomplete
so any ODE solvers requiring the Jacobian would either fail, diverge or produce
incorrect results. It is not clear if many or any parts of the
solidChemistryModel are correct, in particular there is no handling for the
solid surface area per unit volume. After a lot of refactoring work it has
become clear that solidChemistryModel needs a complete rewrite and can benefit
from all the recent development work done on the now more general
StandardChemistryModel.
kappa is now obtained from the fluidThermo for laminar regions, the turbulence
model for turbulent regions and the solidThermo for solid regions. The "lookup"
option previously supported allowed for energy-temperature inconsistent and
incorrect specification of kappa and was not used. Without this incorrect
option there is now no need to specify a kappaMethod thus significantly
simplifying the use boundary conditions derived from temperatureCoupledBase.
