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February 12, 2018, 17:09 |
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#1 | |
Senior Member
Yuehan
Join Date: Nov 2012
Posts: 142
Rep Power: 13 |
Hi,
When I enable 'pseudo transient', the Courant number disappears in the Control tab. What is the essential difference between pseudo-transient and steady-state for coupled pressure based solve in Fluent? Thank you! Quote:
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July 3, 2022, 10:53 |
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#2 | |
New Member
Ahmad Hijazi
Join Date: Jul 2022
Posts: 7
Rep Power: 3 |
Quote:
Can I use a flow courant number equals to 1 since it is giving better results than the default number 200 ? |
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March 26, 2013, 09:52 |
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#3 | |
Senior Member
OJ
Join Date: Apr 2012
Location: United Kindom
Posts: 473
Rep Power: 20 |
Quote:
The algebraic approaximation of integral balance for any control volume is given as: Patankar (1980,1981) proposed the underrelaxation factor as This is same as equation 20-60 in ANSYS Help documentation of FLUENT. The implementation of CFL in this context is: or, Consequently the governing equation for the control volume becomes: One may wonder why bother using CFL instead of , when the governing equation is same. But a little observation will bring clarity such that the equation advances in time , where . In case of steady state, this formulation can be used in with pseudo transient solver. Thus CFL represents a more intuitive definition of implicit underrelaxation. Essentially, use of CFL helps advance the solution by multiples of timesteps defined by cell Courant number (the original one, not solver). Essentially, for smaller timestep, the coefficient will be large and solution will be slow, universally. The multiple of CFL helps in keeping timesteps different in different regions of the domain, with different values of , instead of employing a singular timescale over whole domain. Thus timestep becomes location specific and is different throughout the domain. This helps in convergence, because in case of single universal timestep, its value may be too small somewhere (in case of higher velocities) so the solution in this region will progress slow in time or too large elsewhere (in regions of small velocities) so the solution in this region may just diverge inducing instability. One of the most important aspect of using this formulation instead of under relaxation factor is that with CFL you have a wider range of advancement factors. Under relaxation factors of 0.9,0.95 and 0.99 imply CFL values of 9, 19, 99 respectively. Thus use of CFL gives a wider (or refined) range of pace-change than URF. Higher values of CFL will advance the solution with larger timesteps, increasing pace of solution. But it is wise to do it gradually than suddenly. OJ |
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April 13, 2013, 11:36 |
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#4 |
Senior Member
François Grégoire
Join Date: Jan 2010
Location: Canada
Posts: 392
Rep Power: 17 |
Quote:
Thanks for the theory! But there is still something I don't understand: when we adjust the Flow Courant Number (under Solution Controls), why can we still adjust the URFs? The way I see the equations, the solver uses either the CFL formulation or the formulation. Why can we adjust both? |
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April 19, 2014, 07:02 |
clarification
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#5 |
Senior Member
Join Date: Mar 2010
Posts: 173
Rep Power: 17 |
Dear OJ,
Thanks very much for this post. It is very helpful Could i just ask a few additional questions if possible? According to some documentation i found on the web produced by ANSYS, the Courant No. in the context of the PBCS in Fluent affects the diagonal dominance of the coefficient matrix, and therefore the solution stability - and this is clear in the context of linear solver convergence theory etc. Effectively, this does the same thing as the implicit URF's in the segregated solvers ... However, in one of your posts below, you mention the explicit under-relaxation (relaxation of variables) affects the inner loops of the PBCS? Could i ask you to clarify this further? Do you mean the linear solver loops? i.e. PBiCG solver loops etc? Or where exactly in the algorithm are the explicit URF's applied? I know in OpenFOAM, for instance, in their SIMPLE implmentation, they use explicit under-relaxation for the pressure equation, but implicit (equation) URF's for MOM, TKE and Eps etc. I wonder if you would mind explaining this a little further? Also, in your current (this) post, you use the following nomenclature: I was wondering whether you could just explain your nonemclature? obviously is time ... is cell-volume, i.e. mesh size? Also i am assuming is some sort of global time step?? Quote:
Finally - could you comment on how the explicit URF's affect the simulation behaviour? As per above, i know Courant No. in this context affects the convergence stability - how then do the explicit URFs participate? Are they related somehow to the need to deal with the governing equation non-linearities? Again, thanks very much for the post, best regards Jonathan Last edited by Jonathan; April 22, 2014 at 10:56. |
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March 26, 2013, 06:38 |
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#6 | |
Super Moderator
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Quote:
For transient case PISO and coupled are good option as they can accommodate larger time steps... And I would prefer coupled. Still not checked the results, accuracy and speed of these two schemes... |
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Tags |
cfl, coupled, courant, under-relaxation factor |
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