|
[Sponsors] |
July 16, 2013, 04:10 |
solution is not getting converged
|
#1 |
New Member
Nijanthan Thinakaran
Join Date: Jul 2013
Posts: 15
Rep Power: 13 |
am having pressure inlet of 83 bar,where its inlet diameter is of 9.05mm. also pressure outlet of 43 bar with outlet dia of 2.05mm.
my problem is if i monitor the mass flow rate in inlet it is around e15. because of which my solution is getting diverged and also am having turbulence viscosity limited error. how do i rectify it ??? Note: msh count is of 6.4million and it has interfaces in it. |
|
July 22, 2013, 09:40 |
|
#2 |
Senior Member
Paritosh Vasava
Join Date: Oct 2012
Location: Lappeenranta, Finland
Posts: 732
Rep Power: 23 |
83 bar (almost 38 atm) and a diameter of mere 9 mm looks an unrealistic problem. What is the application of your problem?
|
|
July 24, 2013, 05:52 |
injector
|
#3 |
New Member
Nijanthan Thinakaran
Join Date: Jul 2013
Posts: 15
Rep Power: 13 |
well its kind of water injector. sorry sir cant tel rest of it coz its confidential
|
|
July 24, 2013, 08:37 |
|
#4 |
Senior Member
Paritosh Vasava
Join Date: Oct 2012
Location: Lappeenranta, Finland
Posts: 732
Rep Power: 23 |
Ofcourse with that high pressure you would get high mass flow rate. The turbulence viscosity error is because of coarse mesh, bigger time step or both.
Last edited by vasava; July 25, 2013 at 02:39. |
|
July 24, 2013, 21:35 |
|
#5 |
Member
Join Date: Jul 2013
Posts: 80
Rep Power: 13 |
I'm not sure, but I think that the problem could be that the conditions of pressure-inlet and pressure outlet, it might be too restrictive.
First try with mass-flow-inlet and presure outlet and if it doesn't still work, try mass-flow-inlet and outflow. Also use the first order discretization and make sure you have set up your case properly, specially make sure your material choice is the correct one. Best regards. |
|
July 25, 2013, 02:42 |
|
#6 |
Senior Member
Paritosh Vasava
Join Date: Oct 2012
Location: Lappeenranta, Finland
Posts: 732
Rep Power: 23 |
Still my concern is the enormous amount of pressure and the tiny little outlet. You would need billions of mesh elements just to keep the courant number low.
There must be some other detail you can spare. |
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
simple solution converged in 9 iterations? | Gabbee90 | OpenFOAM Running, Solving & CFD | 4 | January 29, 2019 22:04 |
smoothSolver diverges - solution in using PBiCG solver? | makaveli_lcf | OpenFOAM Running, Solving & CFD | 3 | September 11, 2013 13:44 |
New sixDoFRigidBody BC working with laplaceFaceDecomposition | Ya_Squall2010 | OpenFOAM Running, Solving & CFD | 13 | April 17, 2013 03:04 |
residual plot after solution reset | plaunie | STAR-CCM+ | 1 | April 3, 2010 07:53 |
Does FOAM converge to exact solution in Laplace equation? | santiagomarquezd | OpenFOAM Running, Solving & CFD | 0 | March 26, 2010 08:52 |