|
[Sponsors] |
Error: Static Temperature didi not converge on faces on outlet |
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
December 21, 2019, 13:09 |
Error: Static Temperature didi not converge on faces on outlet
|
#1 |
New Member
Amey Raju Pawade
Join Date: May 2019
Posts: 7
Rep Power: 7 |
Hello,
I am simulating a flow through a cooling jacket of motor. The fluid path is spiral along the circumference of the motor with inlet and outlets. I am using the Segregated Flow and Energy model, BC's are mass flow inlet with a Total temperature of 303 K and at outlet - Pressure outlet with a Static temperature of 340 K. The inner wall of jacket has a heat source and it is a Conjugate Heat transfer simulation which I am running with solid region as transient state and fluid region as steady state. The energy residuals of fluid region has converged and are in the range of 10^-6 and I am also monitoring the pressure drop which is also kind of constant, and hence can be said converged. But the aforementioned error still exists after a long time even though energy residuals are low. Error message : Static temperature did not converge 588 times on model-part "Outlet" Static temperature did not converge 4094795 times on model-part "Fluid Region" Why is this happening and what does this error exactly mean? Thank you. |
|
December 23, 2019, 10:30 |
|
#2 |
Senior Member
Matt
Join Date: Aug 2014
Posts: 947
Rep Power: 18 |
Basically, the solver doesn't like your choice of boundary conditions. It doesn't play well with the outflow you have described. When you see something like this its a good bet that your boundary conditions are at fault.
You might try changing the pressure outlet option to 'radial equilibrium'. This is better suited for rotational (or spiral) outflow as you have described. I also tend to stay away from the segregated solver for thermal problems. Try switching to the coupled solver and see if that doesn't also help. Good luck. These sorts of errors can be tough to chase down sometimes. |
|
December 25, 2019, 14:04 |
|
#3 |
New Member
Amey Raju Pawade
Join Date: May 2019
Posts: 7
Rep Power: 7 |
Hi, Thank you for replying.
But I don't think that the radial equilibrium BC is available in Star-CCM, but can I add a target mass flow at the pressure outlet boundary? Will that in any way affect the stability? One more question I have is, should I trust this solution as the energy residuals are down to the magnitude of -6? Also, one thing I observed is - When I run just the solid region with the specified heat source on the inner wall, the temperature of that wall at a steady state is near about 2000 K, which I cross-checked with manual calculations. But while running CHT, the temperature at the inner wall does not go that high, it is highest at the start - value being the static temperature at which it is initialized (800 K), and then decreases there onwards. |
|
January 4, 2020, 06:59 |
|
#4 | |
New Member
Amey Raju Pawade
Join Date: May 2019
Posts: 7
Rep Power: 7 |
Quote:
|
||
Tags |
conjugate heat transfer, fluid dynamics, star ccm+ |
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Foam::error::PrintStack | almir | OpenFOAM Running, Solving & CFD | 92 | May 21, 2024 08:56 |
parallel run OpenFoam | Srinath Reddy | OpenFOAM Running, Solving & CFD | 13 | February 27, 2019 10:15 |
[Other] Mesh Importing Problem | cuteapathy | ANSYS Meshing & Geometry | 2 | June 24, 2017 06:29 |
[snappyHexMesh] SnappyHexMesh for internal Flow | vishwa | OpenFOAM Meshing & Mesh Conversion | 24 | June 27, 2016 09:54 |
[Commercial meshers] fluentMeshToFoam multidomain mesh conversion problem | Attesz | OpenFOAM Meshing & Mesh Conversion | 12 | May 2, 2013 11:52 |