|
[Sponsors] |
![]() |
![]() |
#1 |
New Member
ivan
Join Date: Dec 2014
Posts: 14
Rep Power: 10 ![]() |
Hi guys, im new in CFX and im trying to simulate a gas liquid multiphase flow but im getting weird results, i just want to be able to identify some horizontal pipe flow patterns (wave, stratified, etc) but i reallt dont know very well how to set the bc and multiphase models, i have read some tutorial and i have done this.
i set a simple horizontal pipe 3 m lenght and 0.20 m diameter at inlet i set 0.5 of gas and 0.5 of water 1 m/s both a simple outlet with av pressure 0 atm im starting with laminar flow, both continuos phases, inhomogeneuos. fluid pair with mixing model, and drag coefficient. i just want to know what best settings i have to usea to model stratified flow as i run the model i get some waves but at some time i have "picks" in convergence and i see like suddenly "explosions" in the flow. i know i have alotof things wrong. In simple words what a have to do to set a stable model. |
|
![]() |
![]() |
![]() |
![]() |
#2 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,327
Rep Power: 138 ![]() ![]() ![]() ![]() |
For free surface flows - they are quite sensitive to time step size. I would recommend you use adaptive time stepping so it can automatically find a good time step.
Use adaptive time stepping, homing in on 3-5 coeff loops per iteration. Make sure the max and min time step size are wide enough that you do not hit them, and give it a sensible starting time step size. |
|
![]() |
![]() |
![]() |
![]() |
#3 |
New Member
ivan
Join Date: Dec 2014
Posts: 14
Rep Power: 10 ![]() |
thanks glenn ill try that today.
|
|
![]() |
![]() |
![]() |
![]() |
#4 |
Senior Member
Mr CFD
Join Date: Jun 2012
Location: Britain
Posts: 361
Rep Power: 13 ![]() |
Curious question for the knowledgeable:
Can you run this problem in steady state, with a small physical time step (e.g. t = 0.001 s) for 10000 iterations? This will give you a pseudo simulation time of 0.001 * 10000 = 10 s. Then use the steady state results as the initial guess for a transient run, but setting the initial start time as 10 s? Thanks |
|
![]() |
![]() |
![]() |
Tags |
gas, liquid, multiphase flow |
Thread Tools | Search this Thread |
Display Modes | |
|
|
![]() |
||||
Thread | Thread Starter | Forum | Replies | Last Post |
sonicFoam - pressure driven pipe: flow continuity violation and waveTransmissive BC | Endel | OpenFOAM Running, Solving & CFD | 3 | September 11, 2014 16:29 |
Imposing gas and liquid mass flow rate BC for hyperbolic equations | omid1361 | Main CFD Forum | 0 | October 17, 2012 02:07 |
Gas solid flow in a pipe with 90 bend | pandaba | FLUENT | 0 | September 14, 2010 01:43 |
What is the difference between liquid reactive flow and gas reactive flow? | James | Main CFD Forum | 6 | May 15, 2009 12:14 |
Two-Phase Buoyant Flow Issue | Miguel Baritto | CFX | 4 | August 31, 2006 12:02 |