|
[Sponsors] |
March 30, 2011, 03:25 |
|
#21 |
Senior Member
Join Date: Mar 2011
Posts: 158
Rep Power: 15 |
Hello,
I have another question to -k=turbulent energy -epsilon=dissipation -nut=turbulent viscosity I have to set up these files in the 0-file as boundary cinditions. k and epsilon must have a value for the inlet surfaces. But how can I calculate these values? And what is meant with the values Cmu 0.09; kappa 0.41; E 9.8; They are automatically set up as written above. What do they mean? Best Regards, tH3f0rC3 |
|
March 30, 2011, 11:58 |
|
#22 |
New Member
Fatih
Join Date: Sep 2010
Location: Hamburg
Posts: 12
Rep Power: 16 |
hi dirk,
may be this will help you http://www.cfd-online.com/Wiki/Turbu...ary_conditions the other values are default model coefficients which i would not change. |
|
March 30, 2011, 12:34 |
|
#23 |
Senior Member
Join Date: Mar 2011
Posts: 158
Rep Power: 15 |
Hi,
thank you, that's a very good link! :-) |
|
March 31, 2011, 04:34 |
|
#24 |
Senior Member
Join Date: Mar 2011
Posts: 158
Rep Power: 15 |
In the description is written that k and epsilon must be specified for the inlet boundaries.
But how do I set up the walls or outlets? The suggestion of ANSA is to set zeroGradient to walls and outlets. ANSA suggests this by outputting the file as an OpenFoam case. So i don't know if this is right. Another question is how to set up inlet and outlet layers in nut. For walls I can use nutwallfunction but what shall I use for inlet and outlets. The suggestion of ANSA in this case is also zeroGradient. Best Regards, tH3f0rC3 Last edited by tH3f0rC3; March 31, 2011 at 04:59. |
|
March 31, 2011, 07:50 |
|
#25 |
New Member
Fatih
Join Date: Sep 2010
Location: Hamburg
Posts: 12
Rep Power: 16 |
hi dirk,
i would use for k and epsilon: ... outlet { type inletOutlet; inletValue $internalField; // or you calculate with estimated values value $internalField; // only a placeholder } ... and for nut: "(inlet|outlet)" // so you specify inlet AND outlet at the same time { type calculated; } for walls you can use wall function for k and epsilon "(wallA|wallB|wallC)" { type kqRWallFunction; // wall function for k, q and R } and wall { type epsilonWallFunction; } This is for incompressible simulation!!! If you are fluid is compressible than you have to set type compressible::"Wall_Function"; |
|
August 18, 2011, 12:55 |
|
#26 | |
Member
A. Bernath
Join Date: Jun 2011
Location: Karlsruhe, Germany
Posts: 39
Rep Power: 15 |
Quote:
Maybe that helps someone... |
||
August 25, 2011, 11:42 |
Change pressure
|
#27 |
New Member
Peter
Join Date: Feb 2011
Posts: 13
Rep Power: 15 |
You probably have a zero pressure at the internalField. Any how, I got the same message and it went away when I was changing the internal pressure and pressure at outlet.
Gr Peter |
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Heat transfer problem | seojaho | CFX | 6 | May 6, 2010 01:32 |
Heat Transfer Coefficient | los | OpenFOAM Running, Solving & CFD | 5 | January 31, 2010 18:44 |
Which Heat transfer coeffcient to use? | tengra | FLUENT | 1 | May 1, 2009 14:49 |
No results for solid domain | Gary Holland | CFX | 10 | March 13, 2009 04:30 |
Convective Heat Transfer - Heat Exchanger | Mark | CFX | 6 | November 15, 2004 16:55 |