CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > OpenFOAM > OpenFOAM Running, Solving & CFD

LES of turbulent channel flows

Register Blogs Community New Posts Updated Threads Search

Like Tree24Likes

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   February 19, 2009, 12:38
Default Hi Jianying and Ning, I jus
  #41
Senior Member
 
Cedric DUPRAT
Join Date: Mar 2009
Location: Nantes, France
Posts: 195
Rep Power: 17
cedric_duprat is on a distinguished road
Hi Jianying and Ning,

I just want to add that the reference DNS calculation we used to compare our calculation was done with a second order code (in both time and space).
So if you use (real) second order scheme with an accurate mesh, there are no reason to get DNS data.

You can check easily your mesh (close to the wall) but for the numerics .... I don't know.

Cedric
cedric_duprat is offline   Reply With Quote

Old   February 19, 2009, 16:53
Default Hi Cedric: Obviously if you
  #42
Member
 
Ning Yang
Join Date: Mar 2009
Location: University Park, PA, USA
Posts: 84
Rep Power: 17
nzy102 is on a distinguished road
Hi Cedric:

Obviously if you refine the grid, you should be able to get better results. I compared my data with Moser's data, published in physics of fluids. I don't think they use a second-order code.

Ning
nzy102 is offline   Reply With Quote

Old   February 19, 2009, 16:54
Default Hi Cedric: Obviously if you
  #43
Member
 
Ning Yang
Join Date: Mar 2009
Location: University Park, PA, USA
Posts: 84
Rep Power: 17
nzy102 is on a distinguished road
Hi Cedric:

Obviously if you refine the grid, you should be able to get better results. I compared my data with Moser's data, published in physics of fluids (1999). I don't think they use a second-order code.

Ning
nzy102 is offline   Reply With Quote

Old   February 19, 2009, 20:39
Default Hi Ning I tried the one equat
  #44
New Member
 
Jianying Jiao
Join Date: Mar 2009
Posts: 6
Rep Power: 17
jiao is on a distinguished road
Hi Ning
I tried the one equation model, smagorinsky, and dynsmagorinsky, but above my results used the dynsmagorinsky model, not smagorinsky model. my results of dynsmagorinsky model is better than one equation model.
my mesh is poorer than yours, but others are the same as yours.

Hi Cedric
My results isn't better than DNS data, I know my mesh is poor. If increasing mesh, the time of computation increases. If a third-order of the temporal discretization term is used, the time of computation is less than the time of computation of a second-order of the temporal discretization term and increasing mesh.

gave me some advices.
Jianying
jiao is offline   Reply With Quote

Old   February 19, 2009, 20:57
Default Hi Ning I tried the one equat
  #45
New Member
 
Jianying Jiao
Join Date: Mar 2009
Posts: 6
Rep Power: 17
jiao is on a distinguished road
Hi Ning
I tried the one equation model, smagorinsky, and dynsmagorinsky, but above my results used the dynsmagorinsky model, not smagorinsky model. my results of dynsmagorinsky model is better than one equation model.
my mesh is poorer than yours, but others are the same as yours.

Hi Cedric
My results isn't better than DNS data, I know my mesh is poor. If increasing mesh, the time of computation increases. If a third-order of the temporal discretization term is used, the time of computation is less than the time of computation of a second-order of the temporal discretization term and increasing mesh.

gave me some advices.
Jianying
jiao is offline   Reply With Quote

Old   February 26, 2009, 20:45
Default Has anybody tried Re_tau = 180
  #46
sek
Member
 
Sung-Eun Kim
Join Date: Mar 2009
Posts: 76
Rep Power: 17
sek is on a distinguished road
Has anybody tried Re_tau = 180?
sek is offline   Reply With Quote

Old   February 26, 2009, 22:07
Default Just Curious... I'm a complete
  #47
New Member
 
Santosh KC
Join Date: Mar 2009
Location: Norman, Oklahoma, United States
Posts: 2
Rep Power: 0
santosh is on a distinguished road
Just Curious... I'm a complete newbie out here.. Is there any tutorial to get started with DNS/LES of Channel Flow?? What machines do you guys run your code on???
santosh is offline   Reply With Quote

Old   May 13, 2009, 00:49
Default
  #48
Senior Member
 
N/A
Join Date: Mar 2009
Posts: 189
Rep Power: 17
harishg is on a distinguished road
I tried the Re_tau=180 case and it produced acceptable results. I did some analysis at Re_tau=395 using one eq eddy and dyn one eq model. The results obtained using the localized dynamic one equation model was much better than the one eq case with Van Driest damping on a 64 cube grid with 2pi*2*pi domain and the same numerical discretization as the tutorial. Has anyone tried using their own filter width expression instead of the smooth/cuberoolvol filter ? Also majority of the papers which i came across used higher order schemes with LES and that can be another reason for the problem.

Last edited by harishg; May 13, 2009 at 12:49.
harishg is offline   Reply With Quote

Old   May 27, 2009, 07:21
Default
  #49
Senior Member
 
sega's Avatar
 
Sebastian Gatzka
Join Date: Mar 2009
Location: Frankfurt, Germany
Posts: 729
Rep Power: 20
sega is on a distinguished road
Quote:
Originally Posted by cedric_duprat View Post
the time discretisation is Crank-Nicholson. (I think it's backward in the tutorial).
For the numerical scheme I using only central diffential scheme (to keep second order accurate).
so there is no limitedLinear 1 for these terms (div(phi,k), div(phi,B))
Then, the time step is different to keep Co number less than 0.4.
For the solver, I'm using ICCG to solve the pressure (and the same PISO as the tutorial) and BICCG for the other quantities, which is quite different from the tutorial also.
Dear Cedric.

You say you are NOT using limitedLinear 1 for the two terms mentioned.
Can you tell me which one you are using?
Ore actually post your fvSchemes dictionary?

I'm having some problem using oneEqEddy in a square duct LES.
My results are poor and Smagorinsky is far better ...
I don't think thats correct ...

Have a nice day. Sebastian
__________________
Schrödingers wife: "What did you do to the cat? It's half dead!"
sega is offline   Reply With Quote

Old   May 29, 2009, 04:54
Default
  #50
Senior Member
 
sega's Avatar
 
Sebastian Gatzka
Join Date: Mar 2009
Location: Frankfurt, Germany
Posts: 729
Rep Power: 20
sega is on a distinguished road
Hello World.

As mentioned above I am doing the channel flow simulation in a square duct with cyclic bc's for in- and outflow.
My Resolution is 56x56x70 with refined mesh towards the wall so there are 7 cells within y+ < 10.

I'm using two different LES models, namely
  • Smagorinsky (SMG)
  • One Equation Eddy
with two different filter-widths (Delta) each time, namely
  • Cube Root Volume (CRV)
  • van Driest Damping
Well, the results with Smagorinsky are looking more or less good, the results with the One Equation Eddy are scrap.

I'm even experiencing that the velocity profile is not symmetric.
Unfortunately the asymmetry looks to be getting worse when simulation longer and thus doing longer averaging.

Important information on how these plots are obtained: I'm using my own post-processing tool for averaging in the flow-direction (with MATLAB). I'm not primary doubting my own tool, but is there an OpenFOAM tool for post-processing a square duct channel?

Any ideas why the One Equation model is so bad compared to both DNS and Smagorinsky? Well, I expected vice versa.
Attached Images
File Type: jpg UMean_oneEqnEddy.jpg (30.5 KB, 269 views)
File Type: jpg UMean_SMG.jpg (25.4 KB, 209 views)
__________________
Schrödingers wife: "What did you do to the cat? It's half dead!"
sega is offline   Reply With Quote

Old   May 31, 2009, 12:48
Default
  #51
Senior Member
 
sega's Avatar
 
Sebastian Gatzka
Join Date: Mar 2009
Location: Frankfurt, Germany
Posts: 729
Rep Power: 20
sega is on a distinguished road
Quote:
Originally Posted by philippebv View Post
you use the final pressure gradient in the channel to get Tau_w and then U_tau?
I would like to know what is meant by the final pressure gradient?
Is this the averaged pressure gradient at the end of the simulation?
__________________
Schrödingers wife: "What did you do to the cat? It's half dead!"
sega is offline   Reply With Quote

Old   June 3, 2009, 08:00
Default
  #52
Senior Member
 
lakeat's Avatar
 
Daniel WEI (老魏)
Join Date: Mar 2009
Location: Beijing, China
Posts: 689
Blog Entries: 9
Rep Power: 21
lakeat is on a distinguished road
Send a message via Skype™ to lakeat
I guess he meant gradP.raw
__________________
~
Daniel WEI
-------------
Boeing Research & Technology - China
Beijing, China
Email
lakeat is offline   Reply With Quote

Old   June 3, 2009, 08:20
Default
  #53
Senior Member
 
sega's Avatar
 
Sebastian Gatzka
Join Date: Mar 2009
Location: Frankfurt, Germany
Posts: 729
Rep Power: 20
sega is on a distinguished road
Quote:
Originally Posted by lakeat View Post
gradP.raw
Which is written in the last uniform sub-directory of the last time-step?
Just to make sure ...
__________________
Schrödingers wife: "What did you do to the cat? It's half dead!"
sega is offline   Reply With Quote

Old   June 3, 2009, 08:58
Default
  #54
Senior Member
 
lakeat's Avatar
 
Daniel WEI (老魏)
Join Date: Mar 2009
Location: Beijing, China
Posts: 689
Blog Entries: 9
Rep Power: 21
lakeat is on a distinguished road
Send a message via Skype™ to lakeat
Your objective is?? Why do you care about it?
__________________
~
Daniel WEI
-------------
Boeing Research & Technology - China
Beijing, China
Email
lakeat is offline   Reply With Quote

Old   June 3, 2009, 09:03
Default
  #55
Senior Member
 
sega's Avatar
 
Sebastian Gatzka
Join Date: Mar 2009
Location: Frankfurt, Germany
Posts: 729
Rep Power: 20
sega is on a distinguished road
Quote:
Originally Posted by lakeat View Post
Your objective is?? Why do you care about it?
I think you have read my previous posts and know I'm having some difficulties with my LES simulations. Just to make sure I'm not getting something wrong on the way (for example how and where to read gradP to get utau) I'm just asking.
__________________
Schrödingers wife: "What did you do to the cat? It's half dead!"
sega is offline   Reply With Quote

Old   June 3, 2009, 09:16
Default
  #56
Senior Member
 
lakeat's Avatar
 
Daniel WEI (老魏)
Join Date: Mar 2009
Location: Beijing, China
Posts: 689
Blog Entries: 9
Rep Power: 21
lakeat is on a distinguished road
Send a message via Skype™ to lakeat
Am I missing something??? As I remember, I have never used gradP to get U_tau.
__________________
~
Daniel WEI
-------------
Boeing Research & Technology - China
Beijing, China
Email
lakeat is offline   Reply With Quote

Old   June 3, 2009, 09:25
Default
  #57
Senior Member
 
sega's Avatar
 
Sebastian Gatzka
Join Date: Mar 2009
Location: Frankfurt, Germany
Posts: 729
Rep Power: 20
sega is on a distinguished road
Quote:
Originally Posted by lakeat View Post
Am I missing something??? As I remember, I have never used gradP to get U_tau.
Well, but I do.

utau = sqrt( -D/(4*rho) * gradP )

with D beeing the diameter of the Duct.
__________________
Schrödingers wife: "What did you do to the cat? It's half dead!"
sega is offline   Reply With Quote

Old   June 3, 2009, 09:41
Default
  #58
Senior Member
 
lakeat's Avatar
 
Daniel WEI (老魏)
Join Date: Mar 2009
Location: Beijing, China
Posts: 689
Blog Entries: 9
Rep Power: 21
lakeat is on a distinguished road
Send a message via Skype™ to lakeat
I see. ......
I calculate u_taw from a wallShearStress utility, of cause in an averaging sense.

^^^^^^^^^
I guess they are the same, since the essence are the same, right?
__________________
~
Daniel WEI
-------------
Boeing Research & Technology - China
Beijing, China
Email
lakeat is offline   Reply With Quote

Old   June 3, 2009, 10:14
Default
  #59
Senior Member
 
sega's Avatar
 
Sebastian Gatzka
Join Date: Mar 2009
Location: Frankfurt, Germany
Posts: 729
Rep Power: 20
sega is on a distinguished road
Quote:
Originally Posted by lakeat View Post
I guess they are the same, since the essence are the same, right?
I hope so ...
__________________
Schrödingers wife: "What did you do to the cat? It's half dead!"
sega is offline   Reply With Quote

Old   June 16, 2009, 03:26
Default
  #60
Senior Member
 
lakeat's Avatar
 
Daniel WEI (老魏)
Join Date: Mar 2009
Location: Beijing, China
Posts: 689
Blog Entries: 9
Rep Power: 21
lakeat is on a distinguished road
Send a message via Skype™ to lakeat
Hi, can anyone tell me how did you get the U+ versus y+ data?

My results is wrong, so I lost my idea about the procedure...

1. Get wall shear stress
Code:
wallShearStress.boundaryField()[patchi] =
sqrt
(
	nuEff.boundaryField()[patchi]
   *mag(U.boundaryField()[patchi].snGrad())
);
2. Calculate U_tau, (wSS denotes wall shear stress)
Code:
uTau= Foam::sqrt(wSS);
3. Plot U+ versus y+, (nuTmp denotes the value of nuEff)
Code:
scalarField UMeanXPValues = UMeanXvalues/uTau;

makeGraph(y*uTau/nuTmp, UMeanXPValues, "UP", UMean.path(), gFormat);
Is the procedure right?
__________________
~
Daniel WEI
-------------
Boeing Research & Technology - China
Beijing, China
Email
lakeat 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
Pressure inlet boundary conditions for open channel flows jack2000 OpenFOAM Running, Solving & CFD 5 December 6, 2018 11:00
LES In Turbulent in channel flow pankaj saha Main CFD Forum 18 November 20, 2014 05:49
LES In Turbulent in channel flow pankaj saha Main CFD Forum 8 April 15, 2009 11:34
Turbulent channel flow roberthino OpenFOAM Running, Solving & CFD 5 August 15, 2007 08:35
Bc for turbulent channel flow roberthino OpenFOAM Running, Solving & CFD 0 August 13, 2007 08:12


All times are GMT -4. The time now is 21:44.