|
[Sponsors] |
March 31, 2021, 09:28 |
DILUBiCGStab Solving for Pressure always zero
|
#1 |
New Member
Dominik Mütter
Join Date: Mar 2021
Location: Europe
Posts: 4
Rep Power: 5 |
Good day Ladies and Gentlemen,
I would kindly like to ask for your help with an openfoam simulation for my bachelor thesis. I am trying to simulate an oloid stirrerı, using the overPimpleDyMFoam solver with a tabulated six-degree-of-freedom motion. Please be lenient with any stupid mistakes in my setup, I am using Openfoam for roughly half a year now, and CFD in general for only a little bit longer. More detailed description: The case setup is derived from the examples for the overPimpleDyMFoam and pimpleFoam solvers (although I have consulted numerous other sources). The spherical refinement zone together with the oloid is the moving overset part (please note attached images). I have no in- or outflow and no free surface. Problem: Openfoam calculates the flow field U for the oloid, but there is no pressure gradient, and the impulse does not propagate through the whole fluid (as you can see in the image). I have the feeling there is a very simple but stupid mistake in my setup. Code:
Overset analysis : nCells : 2281489 calculated : 343000 interpolated : 0 (interpolated from local:0 mixed local/remote:0 remote:0) hole : 1938489 Overset analysis : nCells : 2281489 calculated : 343000 interpolated : 0 (interpolated from local:0 mixed local/remote:0 remote:0) hole : 1938489 DICPCG: Solving for pcorr, Initial residual = 1, Final residual = 0.00833108, No Iterations 115 PIMPLE: iteration 1 DILUPBiCGStab: Solving for p, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0, global = 0, cumulative = 0 DILUPBiCGStab: Solving for p, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0, global = 0, cumulative = 0 DICPCG: Solving for pcorr, Initial residual = 1, Final residual = 0.00833108, No Iterations 115 PIMPLE: iteration 1 DILUPBiCGStab: Solving for p, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0, global = 0, cumulative = 0 PIMPLE: iteration 2 DILUPBiCGStab: Solving for p, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0, global = 0, cumulative = 0 DILUPBiCGStab: Solving for p, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCGStab: Solving for p, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0, global = 0, cumulative = 0 time step continuity errors : sum local = 0, global = 0, cumulative = 0 DILUPBiCGStab: Solving for p, Initial residual = 0, Final residual = 0, No Iterations 0 DILUPBiCGStab: Solving for p, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0, global = 0, cumulative = 0 time step continuity errors : sum local = 0, global = 0, cumulative = 0 PIMPLE: iteration 2 DILUPBiCGStab: Solving for p, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0, global = 0, cumulative = 0 DILUPBiCGStab: Solving for p, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0, global = 0, cumulative = 0 smoothSolver: Solving for epsilon, Initial residual = 0.000967702, Final residual = 3.061e-07, No Iterations 5 DILUPBiCGStab: Solving for p, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0, global = 0, cumulative = 0 smoothSolver: Solving for k, Initial residual = 0.0570797, Final residual = 5.73559e-07, No Iterations 9 ExecutionTime = 1373.21 s ClockTime = 1377 s Courant Number mean: 0 max: 0 deltaT = 0.0159594 Time = 0.0987593 DILUPBiCGStab: Solving for p, Initial residual = 0, Final residual = 0, No Iterations 0 time step continuity errors : sum local = 0, global = 0, cumulative = 0 smoothSolver: Solving for epsilon, Initial residual = 0.000967702, Final residual = 3.061e-07, No Iterations 5 smoothSolver: Solving for k, Initial residual = 0.0570797, Final residual = 5.73559e-07, No Iterations 9 ExecutionTime = 1375.99 s ClockTime = 1381 s Courant Number mean: 0 max: 0 deltaT = 0.0159594 Time = 0.0987593 I created this case with openfoam 2006/2012. I attached all dictionaries (except for the overset), because I have no idea where the error may lie. Any pointers would be highly appreciated. I wish everyone a pleasant Wednesday, Dominik Mütter 1: Looks like this https://www.youtube.com/watch?v=r-lNe9AUwOg https://www.youtube.com/watch?v=0xNWLr1ILJE Edit: upload of updated dictionaries, added console log Last edited by DominikMuetter; April 2, 2021 at 04:19. Reason: More information, updated Dictionaries |
|
April 4, 2024, 06:38 |
|
#2 |
New Member
tomas lopez olocco
Join Date: Dec 2020
Posts: 4
Rep Power: 5 |
I have the same problem, could you find a solution for it?
|
|
Tags |
6dof, overpimpledymfoam, problem, question |
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Pressure Inlet VS velocity Inlet difference | Mohsin | FLUENT | 9 | January 4, 2021 11:34 |
Pressure Inlet Boundary Conditions | Mr.Goodcat | FLUENT | 5 | June 20, 2019 02:47 |
question regarding LES of pipe flow - pimpleFoam | Dan1788 | OpenFOAM Running, Solving & CFD | 37 | December 26, 2017 15:42 |
Calculation of the Governing Equations | Mihail | CFX | 7 | September 7, 2014 07:27 |
Pressure BC for combustion chamber | Giuki | FLUENT | 1 | July 19, 2011 12:35 |