CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > ANSYS > FLUENT

Continuity equation Convergence issue

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   February 21, 2020, 00:58
Default Continuity equation Convergence issue
  #1
Senior Member
 
rupak504's Avatar
 
Lolita
Join Date: Aug 2016
Posts: 118
Rep Power: 10
rupak504 is on a distinguished road
Hello,

I am using Implicit VOF multi-phase model, to simulate a phase change problem. Also, i have a square 2D domain with Non-uniform structured quadrilateral mesh, finer at center and coarser towards ends. I am also using variable Time step size method. PISO for Pressure velocity coupling. and all other at at their default values.

I have given a convergence criteria of 1e-04 for continuity equation and max 200 iterations/timestep, but just after phase change phenomenon, the continuity residual goes up at 1e+02 and gets stable over there.



I don't know what is causing this problem, and what could be the solution ?


any kind of help would be appreciated

regards

Last edited by rupak504; February 21, 2020 at 03:05.
rupak504 is offline   Reply With Quote

Old   February 21, 2020, 05:39
Default Domain extents
  #2
Senior Member
 
vinerm's Avatar
 
Vinerm
Join Date: Jun 2009
Location: Nederland
Posts: 2,946
Blog Entries: 1
Rep Power: 36
vinerm will become famous soon enough
Few more details would be more helpful. Is the domain closed or open; what are the boundary conditions? Which mass-transfer mechanism is being used. And is it liquid->gas or gas->liquid mass transfer? If yes, then you have to ensure either the domain is open or the gas is being modeled as ideal gas.
__________________
Regards,
Vinerm

PM to be used if and only if you do not want something to be shared publicly. PM is considered to be of the least priority.
vinerm is offline   Reply With Quote

Old   February 21, 2020, 07:15
Default
  #3
Senior Member
 
rupak504's Avatar
 
Lolita
Join Date: Aug 2016
Posts: 118
Rep Power: 10
rupak504 is on a distinguished road
Quote:
Originally Posted by vinerm View Post
Few more details would be more helpful. Is the domain closed or open; what are the boundary conditions? Which mass-transfer mechanism is being used. And is it liquid->gas or gas->liquid mass transfer? If yes, then you have to ensure either the domain is open or the gas is being modeled as ideal gas.



Domain is open from top with Pressure outlet boundary condition. All other sides have No-slip BC. Lee model for pool boiling. Liquid to gas mass transfer.
rupak504 is offline   Reply With Quote

Old   February 21, 2020, 07:26
Default Time-step
  #4
Senior Member
 
vinerm's Avatar
 
Vinerm
Join Date: Jun 2009
Location: Nederland
Posts: 2,946
Blog Entries: 1
Rep Power: 36
vinerm will become famous soon enough
One possibility is time-step. If the simulation does not converge within 30-40 iterations in a time-step it implies that the time-step is larger than it ought to be. 200 iterations is not suitable. Even if the simulation converges in, say, 80 or 100 iterations, results will appear jaggered over time. Second point is numerics, i.e., space discretization and URFs. If physical setup is good, you will be able to control the run using numerics and time-step.
__________________
Regards,
Vinerm

PM to be used if and only if you do not want something to be shared publicly. PM is considered to be of the least priority.
vinerm is offline   Reply With Quote

Reply


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
Continuity Equation for multicomponent simulation lordluan CFX 15 May 19, 2020 19:36
Stuck in a Rut- interDyMFoam! xoitx OpenFOAM Running, Solving & CFD 14 March 25, 2016 08:09
IcoFoam parallel woes msrinath80 OpenFOAM Running, Solving & CFD 9 July 22, 2007 03:58
continuity equation Rafal Main CFD Forum 4 November 29, 2006 10:27
Could anybody help me see this error and give help liugx212 OpenFOAM Running, Solving & CFD 3 January 4, 2006 19:07


All times are GMT -4. The time now is 03:44.