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

Correct method for calculating time step size

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   February 9, 2016, 04:49
Default Correct method for calculating time step size
  #1
New Member
 
Aarthy Meena's Avatar
 
Aarthy Meena
Join Date: Oct 2015
Location: Trichy
Posts: 29
Rep Power: 11
Aarthy Meena is on a distinguished road
Hello Everyone,

I am a newbie to FLUENT & CFD. I wanted to calculate time step size for unsteady flow around a circular cylinder of dia = 0.01m in the Reynolds number of 45 to 50. The working fluid is water with viscosity = 0.001003 kg/ms and density = 998.2 kg/m3.

I came across several posts related to this and many methods to calculate the time step size.

1) From Strouhal number (0.2 for circular cylinder- approx)

Sr (0.2) = (frequency x diameter) / velocity
From the above equation find the frequency. The total time period, T = 1/frequency. Hence, time step \Deltat = T/25 (approx).

2) From CFL condition
\Delta t = C_m X \Delta x / velocity
where, C_m = 1 (approx) and \Delta x = minimum cell size.

3)From domain length
\Delta t = domain length / (20 x velocity)

1) Which of the above method is correct ?
2) How to calculate the suitable time step size for my condition?
3) Please explain.

Thanks in advance.
__________________
Aarthy,
PG Student,
National Institute of Technology, Trichy, India.

Last edited by Aarthy Meena; February 9, 2016 at 05:50.
Aarthy Meena is offline   Reply With Quote

Old   February 9, 2016, 05:25
Default
  #2
Senior Member
 
Filippo Maria Denaro
Join Date: Jul 2010
Posts: 6,896
Rep Power: 73
FMDenaro has a spectacular aura aboutFMDenaro has a spectacular aura aboutFMDenaro has a spectacular aura about
the time step is constrained by stability criteria that are based not only on the cfl condition but also on the visicous terms.

Furthermore, each discretization has a specific stability region
FMDenaro is offline   Reply With Quote

Old   February 9, 2016, 05:28
Default
  #3
New Member
 
Aarthy Meena's Avatar
 
Aarthy Meena
Join Date: Oct 2015
Location: Trichy
Posts: 29
Rep Power: 11
Aarthy Meena is on a distinguished road
Dear Sir,

Can you please explain me the method for my flow scenario around a circular cylinder.
__________________
Aarthy,
PG Student,
National Institute of Technology, Trichy, India.
Aarthy Meena is offline   Reply With Quote

Old   February 9, 2016, 05:36
Default
  #4
Senior Member
 
Filippo Maria Denaro
Join Date: Jul 2010
Posts: 6,896
Rep Power: 73
FMDenaro has a spectacular aura aboutFMDenaro has a spectacular aura aboutFMDenaro has a spectacular aura about
The numerical stability depends upon the method you use for the integration and the sizes of the mesh (in all directions), does not depend on a specific flow problem.
Assuming you are using non-dimensional equations, the velocity magnitude is no more than O(1) so that you can use that as estimation in the (multidimensional) CFL condition
FMDenaro is offline   Reply With Quote

Old   February 9, 2016, 05:46
Default
  #5
New Member
 
Aarthy Meena's Avatar
 
Aarthy Meena
Join Date: Oct 2015
Location: Trichy
Posts: 29
Rep Power: 11
Aarthy Meena is on a distinguished road
Thank you sir,

Actually am very new to FLUENT and I do not understand your reply. In FLUENT, I am using dimensional form of the governing equations. Kindly please suggest me some material where I can learn about this topic.
__________________
Aarthy,
PG Student,
National Institute of Technology, Trichy, India.
Aarthy Meena is offline   Reply With Quote

Old   February 10, 2016, 04:20
Default
  #6
New Member
 
Lucas
Join Date: Jun 2015
Posts: 20
Rep Power: 11
Edeluc is on a distinguished road
A theoretical advice:
The CFL-number and the according "condition" are only part of the stability analysis of numerical schemes. A good introduction (for Finite Difference methods) can be found on:
https://en.wikipedia.org/wiki/Von_Ne...ility_analysis

Basically the stability depends on the equation you discretise (including all the terms in it - as FMDemaro added), as well as the discretisation scheme you use. As a "rule of thumb": lower order discretisation schemes (e.g.: Upwind schemes) and implicit time-dependent solution are very stable, whereas the more accurate methods tend to be unstable. For the Finite Element method, this can be proven analytically for certain cases - An example is also contained in the link.

A practical advice:
I am not familiar with ANSYS Fluent but I guess, that you will use Finite Volume Method with an implicit solver. The theoretical advice from above might therefore be tough to prove for your problem. I would advise you to have look on the user manual and see, if there is any hint. A cylinder in cross flow is also very well researched and there might be a lot of data and advice for your example already available.

Regards,
Lucas
Edeluc is offline   Reply With Quote

Old   February 10, 2016, 05:46
Default Help please!!
  #7
New Member
 
Ravi
Join Date: Feb 2016
Posts: 1
Rep Power: 0
r.pdl is on a distinguished road
I am trying to do a transient analysis of flow through a bifurcation of penstock pipe (wye) using ansys cfx . Here i need to specify the conditions that the valves of the turbine are closed within a 5 seconds of time. I thought of giving pressure inlet and mass flow rate at the outlet. Now i need to vary the mass flow rate at the outlet from 4650kg/s to 0 within a 5 seconds of time and i dont know how to do that in ansys CFX. Can anybody help me please ??
r.pdl is offline   Reply With Quote

Old   May 7, 2019, 08:56
Default question
  #8
Member
 
Join Date: Sep 2018
Posts: 31
Rep Power: 8
serrar is on a distinguished road
Dear Aarthy Meena,
did you find a good average to calculate the time step and time step size?
serrar is offline   Reply With Quote

Reply

Tags
circular cylinder, fluent 14.5, time step size, transient simulations


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
AMI speed performance danny123 OpenFOAM 21 October 24, 2020 05:13
time step continuity problem in VAWT simulation lpz_michele OpenFOAM Running, Solving & CFD 5 February 22, 2018 20:50
Star cd es-ice solver error ernarasimman STAR-CD 2 September 12, 2014 01:01
Micro Scale Pore, icoFoam gooya_kabir OpenFOAM Running, Solving & CFD 2 November 2, 2013 14:58
same geometry,structured and unstructured mesh,different behaviour. sharonyue OpenFOAM Running, Solving & CFD 13 January 2, 2013 23:40


All times are GMT -4. The time now is 15:18.