|
[Sponsors] |
![]() |
![]() |
#1 |
Senior Member
Govindaraju
Join Date: Apr 2010
Posts: 209
Rep Power: 17 ![]() |
Dear all
My geometry has a curved pipe. the fluid entering +y direction (inlet as pressure). The outlet axis coordinate has (+x,-y) coordinate. So I introduced outlet (velocity) as Normal to the surface. My question is if I rotate the component in the workbench so that the outlet is along X axis, How about my result in this case and previous case? is it same or different? Thank you Govind |
|
![]() |
![]() |
![]() |
![]() |
#2 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,890
Rep Power: 144 ![]() ![]() ![]() ![]() |
If you rotate the thing and do the same simulation you should expect the same result, just rotated. Is that what you are asking?
Or are you asking if you can use a previous rotated simulation as an initial condition? That is harder - in general, no, you cannot. |
|
![]() |
![]() |
![]() |
![]() |
#3 | |
Senior Member
Govindaraju
Join Date: Apr 2010
Posts: 209
Rep Power: 17 ![]() |
Quote:
I have another question. Please find the attached pictures. I am confusing about turbulence model.I run the steady state first and then transient . My inlet is pressure and outlet is velocity . I am expecting low Reynolds turbulence occurring near the curve and the area restriction . Is my solution is converged or not.I tried SST model .I also tried tried many models like RNG K-epsilon, K-omega etc , but the solution doesn't meet the convergence criteria 10^-4 Give your advice Thank you Govind |
||
![]() |
![]() |
![]() |
![]() |
#4 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,890
Rep Power: 144 ![]() ![]() ![]() ![]() |
||
![]() |
![]() |
![]() |
![]() |
#5 | |
Senior Member
Govindaraju
Join Date: Apr 2010
Posts: 209
Rep Power: 17 ![]() |
Quote:
please find the following statement.U Mom, v-mom, Vmom, P-mass all are F. This will start from 70th iteration t0 100 iteration . what does it mean. Thank you +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 3.8E-04 | 9.5E-03 | 1.0E+00 F | | V-Mom | 1.00 | 3.8E-04 | 7.5E-03 | 1.0E+00 F | | W-Mom | 1.00 | 5.2E-04 | 1.7E-02 | 1.0E+00 F | | P-Mass | 1.00 | 1.0E-04 | 5.4E-03 | 8.9 1.0E+00 F | +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.99 | 8.7E-05 | 4.4E-03 | 5.7 8.1E-02 OK| | O-TurbFreq | 1.05 | 8.3E-06 | 8.6E-04 | 10.5 5.8E-07 OK| +----------------------+------+---------+---------+------------------+ | Rethetat | 2.17 | 6.1E-04 | 2.8E-01 | 5.9 1.0E-02 OK| | Intermit | 0.77 | 6.0E-05 | 1.4E-02 | 5.7 5.8E-03 OK| +----------------------+------+---------+---------+------------------+ ================================================== ==================== OUTER LOOP ITERATION = 88 CPU SECONDS = 2.320E+03 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 3.8E-04 | 9.5E-03 | 1.0E+00 F | | V-Mom | 1.00 | 3.8E-04 | 7.5E-03 | 1.0E+00 F | | W-Mom | 1.00 | 5.2E-04 | 1.7E-02 | 1.0E+00 F | | P-Mass | 1.00 | 1.0E-04 | 5.4E-03 | 8.9 1.0E+00 F | +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.99 | 8.6E-05 | 4.3E-03 | 5.7 8.0E-02 OK| | O-TurbFreq | 1.03 | 8.6E-06 | 9.1E-04 | 10.5 5.3E-07 OK| +----------------------+------+---------+---------+------------------+ | Rethetat | 1.16 | 7.1E-04 | 2.6E-01 | 5.9 1.1E-02 OK| | Intermit | 1.06 | 6.4E-05 | 8.7E-03 | 5.7 7.1E-03 OK| +----------------------+------+---------+---------+------------------+ |
||
![]() |
![]() |
![]() |
![]() |
#6 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,890
Rep Power: 144 ![]() ![]() ![]() ![]() |
This is explained in the documentation. It means the linear solver is diverging. Check that your simulation is correctly setup, improve your mesh quality, use smaller time steps, double precision numerics or a better initial condition.
|
|
![]() |
![]() |
![]() |
Thread Tools | Search this Thread |
Display Modes | |
|
|
![]() |
||||
Thread | Thread Starter | Forum | Replies | Last Post |
transient, impregnating flow problem | fgommer | FLUENT | 0 | February 29, 2012 17:10 |
Non-steady flow simplified for use in Vissim | steamerandy | Main CFD Forum | 0 | October 31, 2011 22:08 |
Fully Developed Flow in Star-cd | SMM | STAR-CD | 0 | September 5, 2011 23:08 |
Flow meter Design | CD adapco Group Marketing | Siemens | 3 | June 21, 2011 09:33 |
transform navier-stokes eq. to euler-eq. | pxyz | Main CFD Forum | 37 | July 7, 2006 09:42 |