|
[Sponsors] |
February 10, 2021, 23:26 |
Laminar model not converging
|
#1 |
New Member
Juan Cisneros
Join Date: Nov 2017
Posts: 3
Rep Power: 9 |
Hello Fluent users,
I am analyzing the hydrodynamic flow in a wastewater treatment reactor with Re = 450. The laminar model was chosen for the simulation. A polyhedra-based mesh with approximately 1.3M cells was generated in fluent meshing. The mesh has an average and maximum skewness of 0.12 and 0.5, respectively. I use the coupled pressure-based solver and second-order upwind discretization schemes. To initialize the simulation, I use hybrid initialization. However, with this setup, I have not been able to get a converged solution, the velocity residuals do not drop below 1e-3, and the continuity residual rises above 0. I am attaching images of the reactor, the baffles, the water inlet, outlet and the residuals. I am looking forward for someone's advice. Cheers Juan reactor.jpg Residuals.png |
|
February 11, 2021, 17:27 |
|
#2 |
New Member
ashkan ghafari
Join Date: Sep 2017
Location: Iran
Posts: 1
Rep Power: 0 |
Hi,
There are some tips you can try : 1- use first-order upwind discretization at the beginning of the simulation. 2- reduce the courant number or urf in the solution control section. 3- use transient solver. |
|
February 12, 2021, 08:32 |
|
#3 |
Senior Member
Lorenzo Galieti
Join Date: Mar 2018
Posts: 375
Rep Power: 12 |
Hi juan,
The mesh is good, so no problem about that. I would only put some more elements in the pipe inlet and extend it a fair bit (6-8 Diameter lengths). You need to have developed flow entering the reactor, place the inlet far away from where interesting stuff happens. This may also help with convergence Apart from that, let me understand better: is there something spinning inside the reactor? Like a sort of propeller? If yes, no wonder the steady simulation doesn't converge |
|
Tags |
convergence failure, fluent - parallel, laminar model |
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Table bounds warnings at: END OF TIME STEP | CFXer | CFX | 4 | July 17, 2020 00:44 |
Eulerian-Eulerian turbulent two-fluid model is not converging? | minzhang | Fluent Multiphase | 26 | April 24, 2020 05:13 |
[swak4Foam] swakExpression not writing to log | alexfells | OpenFOAM Community Contributions | 3 | March 16, 2020 19:19 |
choosing turbulence model for gas phase while laminar model for solid phase | Haiqin | STAR-CCM+ | 3 | July 12, 2016 05:45 |
Is Non premixed combusiton (flamelet model) in Fluent able to calculate laminar? | sooroo3 | FLUENT | 2 | November 10, 2013 06:47 |