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January 4, 2017, 19:38 

#201  
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I have used fvOptions too but it doesn't make any difference. Nevertheless, since I am solving for incompressible flow and because of the continuity, the setAverage option must trigger the required the pressure difference. 

January 4, 2017, 22:28 

#202 
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Elham
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How big is the Re number? Is it in the turbulent limit?


January 6, 2017, 23:23 

#203 
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January 7, 2017, 02:46 

#204 
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Elham
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January 9, 2017, 04:53 

#205 
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bin xu
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hellow
i find that the the result of channel395 in of2.4 is quite different from of3.0. I have changed the Sgs model to dylagragian model in of 2.4 ,and the result seems similar to of 3.0 . i wonder if there is something wrong in oneEqu model in of2.4 ? I think the u_tau should be equal to 0.0079 in channel395 ,but however i changed the settings, my u_tau never got right. I use both ways trying to calculate u_tau 1.u_tau=sqrt(h*dp/dx) 2.u_tau=sqrt(nu*u1/y1),u1 and y1 are data on the first point above the wall. my simulation data are like this sorry for my bad english. hope someone can help me solve this problem. thanks ! 

January 10, 2017, 02:11 

#206 
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Thanks for the suggestion. Yes, it works but the problem is that I don't know the turbulence intensity beforehand and I don't want to use synthetic b.c for the inlet. I think I better stick to a precursor simulation and forget about mapped boundary condition.


February 10, 2017, 14:31 

#207 
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Darko Radenkovic
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Hello.
I did LES Smagorinsky simulation with van Driest damping and I obtained good results, for turbulent flow in channel. Then I wanted to try dynamic model and I tried dynamicKEqn. IAlso I changed delta to cubeRootVol. I kept all other settings the same as for Smagorinsky, which gave good results. I had run simulation for about 90 flowthrough times and after that I started averaging for about 250 flowthrough times. Results are not good (velocity is in file on link below). Does anyone have an idea what could be the reason for discrepancy of this model and log law? Relevant settings are on this link https://www.dropbox.com/s/ct104fg36l...cKEqn.zip?dl=0 Any help is appreciated. Regards, Darko 

February 20, 2017, 21:55 

#208  
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bin xu
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Thanks! Regards, Xu Bin 

February 21, 2017, 03:13 

#209 
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Darko Radenkovic
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Xu Bin,
Keep all settings the same as in my previous attached file, just change delta to vanDriest and LESModel to Smagorinsky. These settings should be the same as settings which can be found in tutorial in folder channel395 in OpenFOAM. Regards, Darko 

February 22, 2017, 03:31 

#210 
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bin xu
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Darko,
how do you calculate u_tau to nondimensionalize u and y to get the u+ and y+ data ? Regards Xu Bin 

February 22, 2017, 04:00 

#211 
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Darko Radenkovic
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Xu Bin,
After using postChannel utility, I calculate friction velocity as $u_tau = \sqrt{\nu \frac{u_{fc}}{y_fc}}$. Index fc denotes first cell, and \nu is kinematic viscosity. About nondimensional distance: https://www.cfdonline.com/Wiki/Dime...tance_(y_plus) Regards, Darko 

March 1, 2017, 03:18 

#212  
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bin xu
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Quote:
do you get the correct u_tau=0.0079 for case channel 395. i find that many people get the result u_tau = 0.73. i also meat the problem.i have tried all approaches to calculated u_tau, the result is still wrong. can you help me ? Regards Xu Bin 

March 2, 2017, 07:03 

#213  
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Jem
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Hey can you tell me how you find the first point above the wall?
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March 20, 2017, 22:20 

#214 
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Elham
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Hi everyone,
I have a turbulent flow in a channel. The channel is 0.3*0.05*0.075m. When I add a stationary 2mm diameter sphere in the domain the turbulent gets laminar quickly. The sphere BC is wall. I suppose the presence of sphere causes the flow to get smooth. How can I have a turbulent flow again? Thanks in advance 

July 13, 2017, 11:32 

#215 
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Hi everyone,
There is one thing I'm very curious. In the beginning of this thread, people compared their LES data obtained from Openfoam with DNS data from Moser et al. I never used openfoam but as far as I know, the accuracy of openfoam is second order in space. But Moser et al. used spectral method for spatial discretization which is more accurate than second order central scheme. If you use the same mesh resolution, you compare your LES result from openfoam with DNS data from Moser et al.,it is reasonable to have some discrepency not only because the difference between LES and DNS, but also because the numerical method in openfoam is less accurate. So why don't you compare your LES result with DNS data which used second order central difference scheme. I did a DNS simulation using an inhouse code which used second order central difference scheme and compare my result with "DNS of turbulent heat transfer in channel flow with respect to Reynolds and Prandtl number effects" from Kawamura et al. In this paper they also used second order central difference scheme so my result matched very well with Kawamura et al. for u+, t+,t't',u'u',v'v',w'w',u't' v't'. So why don't you compare your result with Kawamura et al. but with Moser et al.? Best regards, Wentao Guo 

August 13, 2019, 05:30 

#216  
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Can you help me with something? I tried to run channel395 tutorial case in OpenFoam using channelFoam solver for a larger period of time (i.e. 7000s). What I noticed is that pressure gradient value gradP wobbles over some average value, so I believe simulation can be considered statistically steady state. However, when I tried to calculate uTau from time averaged gradP value ( uTau = sqrt(gradP) ) relative errors (compared to the DNS values) were equal to cca 20% (which is a lot!). The values reported by Eugene in his PhD were much better for similar mesh and same subgridscale models. Did I miss something? P.S. I know Eugene noted in his PhD (page 163) that: To ensure consistency, the streamwise bulk velocity, Ub, through the channel is adjusted to be equal to the average DNS value by varying an imposed streamwise constant pressure gradient, ∂P/∂x. The time averaged value of this quantity is equivalent to the mean wall shear stress and can be compared to the corresponding DNS value. According to that, tau_w should be equal to timeaveraged value of gradP and u_Tau as sqrt(gradP). Or I made some mistake? Thank you! Best regards! 

August 13, 2019, 05:55 

#217  
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Ehsan Asgari
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Just calculate u_tau using the mean velocity. Sure and straight. Regards, Syavash 

August 13, 2019, 06:13 

#218  
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I agree with you. However, theory implies that same uTau value should be obtained from the pressure gradient value. Well, I checked it and I have to say that tau_w can really be calculated from average gradP value. Moreover, I tried to calculate uTau from both, the pressure gradient value and as sqrt(nu*(uc/yc)), where uc is velocity at wall adjacent cell centre and yc is cell centre distance from the wall. The results are basically the same. Best regards! 

August 13, 2019, 11:28 

#219  
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Ehsan Asgari
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Yes, there is a force balance between streamwise pressure gradient and the wall shear stress. However, I usually use the mean velocity profile to calculate the shear stress as you indicated. How is it possible to calculate the mean pressure gradient?! I guess the value written in the last time folder is the instantaneous pressure gradient, is that right? Regards, Syavadh 

August 14, 2019, 09:25 

#220  
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Best regards! 

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