Commit Graph

15 Commits

Author SHA1 Message Date
69d994e794 twoPhaseEulerFoam: Change the implicit particle-pressure and turbulence dispersion
to be phase-symmetric so that the results are independent of which
phase-fraction is solved.
2015-06-25 16:08:21 +01:00
61e52b2cb4 twoPhaseEulerFoam: Move the residualAlpha used for drag into the phaseModel
This is necessary to guarantee consistency between the residualAlpha
used for drag and buoyancy in a multi-phase system
2015-06-07 18:55:24 +01:00
9655398064 twoPhaseEulerFoam: Improvements to implicitPhasePressure 2015-04-28 18:18:34 +01:00
fc6b44ee3c twoPhaseEulerFoam: Added experimental face-based momentum equation formulation
This formulation provides C-grid like pressure-flux staggering on an
unstructured mesh which is hugely beneficial for Euler-Euler multiphase
equations as it allows for all forces to be treated in a consistent
manner on the cell-faces which provides better balance, stability and
accuracy.  However, to achieve face-force consistency the momentum
transport terms must be interpolated to the faces reducing accuracy of
this part of the system but this is offset by the increase in accuracy
of the force-balance.

Currently it is not clear if this face-based momentum equation
formulation is preferable for all Euler-Euler simulations so I have
included it on a switch to allow evaluation and comparison with the
previous cell-based formulation.  To try the new algorithm simply switch
it on, e.g.:

PIMPLE
{
    nOuterCorrectors 3;
    nCorrectors      1;
    nNonOrthogonalCorrectors 0;
    faceMomentum     yes;
}

It is proving particularly good for bubbly flows, eliminating the
staggering patterns often seen in the air velocity field with the
previous algorithm, removing other spurious numerical artifacts in the
velocity fields and improving stability and allowing larger time-steps
For particle-gas flows the advantage is noticeable but not nearly as
pronounced as in the bubbly flow cases.

Please test the new algorithm on your cases and provide feedback.

Henry G. Weller
CFD Direct
2015-04-27 21:33:58 +01:00
f5bb944965 twoPhaseEulerFoam: Improved handling of velocity/flux boundary conditions
Updated tutorials to converge pressure during PIMPLE loop to avoid
phase-fraction unboundedness which limits thermodynamics convergence.
2015-04-12 09:57:56 +01:00
0be1e89204 twoPhaseEulerFoam: Interpolate lift, wall-lubrication and turbulent dispersion forces
Reduces or eliminates staggering patterns due to cell-force imbalances
Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1363
2015-04-08 12:19:23 +01:00
9a40fb787e multiphase solvers: print phase-name rather than alpha1/2 when printing max and min phase-fraction 2015-01-21 20:07:15 +00:00
4b30be42ff BUG: mantis #1365: switched to using wall reflection to calculate wall normals, and added caching of the wall values 2014-08-14 12:45:57 +01:00
85da9e6a54 twoPhaseEulerFoam: Now in fully-conservative form 2014-04-29 15:47:39 +01:00
dd0efd159d twoPhaseEulerFoam: added optional alphaMax to phaseModel for MULES limiter
Resolves bug-report http://www.openfoam.org/mantisbt/view.php?id=1209
2014-03-07 23:32:00 +00:00
2843ceff2f ENH: twoPhaseEulerFoam: made blending methods multiphase, and associated them with model types 2014-01-24 09:09:51 +00:00
509529cab8 ENH: Added bubble library functionality to twoPhaseEulerFoam 2014-01-22 17:46:17 +00:00
475e885772 ENH: Abstracted and made run-time selectable the lift models in twoPhaseEulerFoam 2014-01-02 16:53:37 +00:00
79467c20ae twoPhaseEulerFoam: Added IATE 2013-10-10 16:29:21 +01:00
175f03f87d Removed twoPhaseEulerFoam and renamed compressibleTwoPhaseEulerFoam -> twoPhaseEulerFoam 2013-08-15 10:30:09 +01:00