Changed to using of UPtrList<Type> instead of List<*Type> for storing
reference to size and velocity groups, as this removes de-referencing
clutter. Fixed lookup of critical film thickness in PrinceBlanch
coalescence model. Added functionality calculating the overall diameter,
void fraction and void fraction weighted velocity for multiple velocity
groups.
Patch contributed by Institute of Fluid Dynamics, Helmholtz-Zentrum
Dresden - Rossendorf (HZDR)
This interpolation method was previously removed by commit fbf00209.
The intention of this method is to provide a slip-like wall boundary
condition for the velocity when interpolated to the location of a
Lagrangian element. This is difficult because any velocity which points
through the wall can cause a drag model and a rebound wall interaction
to "fight"; i.e., the drag pushes the particle to the wall, the wall
bounces it back. This can result in the program hanging.
This method extrapolates a vector field to the wall points and then
modifies the result so that it does not point through the wall. It does
this by rotating the vectors towards the (reversed) point normal. The
result is also scaled so that is reduced to zero if the necessary
rotation exceeds 90 degrees.
This provides an alternate resolution to bug report
https://bugs.openfoam.org/view.php?id=2826
Within this structure the BirdCarreau, Casson, CrossPowerLaw, HerschelBulkley,
powerLaw and strainRateFunction strain-dependent viscosity based non-Newtonian
fluid models may be selected for incompressible or compressible flow.
In the case of compressible flow the strain-dependent viscosity functions are
applied to the temperature dependent viscosity so that if the WLF viscosity
model is chosen in conjunction with the CrossPowerLaw the effective model is
Cross-WLF which is commonly used for polymer flow.
These models are selected in the constant/turbulenceProperties file, e.g.
simulationType laminar;
laminar
{
laminarModel generalizedNewtonian;
viscosityModel CrossPowerLaw;
nuInf 10;
m 0.4;
n 3;
}
This new implementation is more general and flexible than the previous
incompressible only non-Newtonian viscosity models, which were selected in the
constant/transportProperties file. This implementation is now deprecated and
will be phased-out.
Description
Transport package using the Williams-Landel-Ferry model.
Templated into a given thermodynamics package (needed for thermal
conductivity).
Dynamic viscosity [kg/m.s]
\f[
\mu = \mu_0 \exp \left(\frac{-C_1 ( T - T_r )}{C_2 + T - T_r}\right)
\f]
References:
\verbatim
Williams, M. L., Landel, R. F., & Ferry, J. D. (1955).
The temperature dependence of relaxation mechanisms
in amorphous polymers and other glass-forming liquids.
Journal of the American Chemical society, 77(14), 3701-3707.
\endverbatim
This fix changes how the intersections loop ignores previously
intersected faces. It now marks them by their index so that subsequent
iterations ignore them.
Before this change, after an intersection was found the start point was
advanced by a small amount to move the past the intersection. The
problem with this was if multiple boundary faces or the end point were
in close proximity to the intersection then the move forward might span
them. This could lead to intersections being missed or counted multiple
times, in some cases indefinitely.
Based on a patch contributed by Mattijs Janssens
Resolves bug report https://bugs.openfoam.org/view.php?id=1147
These options add the ability to show the plot in the terminal, and at
any size. This is intended to facilitate monitoring on remote machines
where launching an X11 application may not be convenient or possible.
Resolves feature request https://bugs.openfoam.org/view.php?id=3080
This provides more flexibility in specifying the allowed internal and boundary
extrema.
For driftFluxFoam and other settling problems it is beneficial to set the
boundaryExtremaCoeff to 1 to allow rapid accumulation of the partials on the
bottom wall (which was the previous default behaviour) but this is not suitable
for many Euler-Euler cases for which a uniform etrema coefficient is preferable,
either 0 or a small value.
Now by default boundaryExtremaCoeff is set to extremaCoeff which defaults to 0
which provides the behaviour before
OpenFOAM-dev commit cb2bc60fa5
and the driftFluxFoam tutorials have been updated adding
boundaryExtremaCoeff 1;
to the MULES controls in fvSolution so reproduce the previous behaviour.
The LBend was set to run for 2 s, but at about 1.95 s the packed region
builds up to the inlet and the simulation diverges. The end time has
been reduced to 1.9 s so that this does not occur.
This change fixes an issue where mass transfer models were being looked
up on the wrong side of the interface. This also means that specifying
mass transfer just on one side of an interface is now possible without
generating errors.
When a part of the tetrahedral decomposition is inverted, tracking along
a straight line can result in a closed loop which never ends.
This change adds a limit to the number of tracks that are done that end
before or at the maximum distance already achieved. This breaks these
closed loops and prevents the simulation from hanging. The particles do,
however, end up in an incorrect position as a result of the tracking
being abandoned at an intermediate point in the step. A warning is
printed to indicate when this is occuring.
This resolves bug report https://bugs.openfoam.org/view.php?id=3056
