CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > General Forums > Main CFD Forum

Initial conditions k and epsilon

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   April 9, 2016, 05:59
Default Initial conditions k and epsilon
  #1
New Member
 
Join Date: Oct 2015
Location: Oviedo, Asturias, Espaņa
Posts: 17
Rep Power: 10
pela145 is on a distinguished road
Hello all!

I have been simulating the effects of the Atmospheric Boundary Layer (ABL) on a 3D high rise building with different Steady RANS turbulence models such as Standard kE, kOmega, kOmegaSST, realizable kE and RNG kE.

I have taken the Cd on the building and the Cp at 2/3H as 2 of my reference values in order to establish a comparation between my simulations with those 5 models and previous similar studies. However, the Cp obtained in all of my calculations is quite larger than those obtained by the mentioned previous studies. Apart from the mesh, which i have already checked and it is not the problem at all, i think that maybe I have used wrong values as the initial conditions of k, omega or epsilon.

My current values are:

turbulent kE: 0.7
turbulent epsilon: 2.0
turbulent omega: 3.0

My inlet U profile is based on a logaritmic law, and reachs 14.5 m/s at the roof. Uy and Uz are zero in the initial conditions.

By the way, I have read about a estimation based on the turbulent intensity. However, since I only use steady RANS models, I cannot estimate that intensity.


Are my initial values good? How should I change them if not? Do you know any way of estimate them?



Thank you all

Any advise will be absolutely helpful.
pela145 is offline   Reply With Quote

Old   April 15, 2016, 02:04
Default
  #2
Senior Member
 
david
Join Date: Oct 2012
Posts: 142
Rep Power: 13
davidwilcox is on a distinguished road
if you are using the log-law for velocity, then k and epsilon have to follow the formulations of the loglaw. Note that the loglaw is the balance between production of k and epsilon. in other words, uv du/dy = epsilon . Epsilon here has a y dependence which means you cannot assign it a fixed value. epsilon in the log-law ( local equilibrium) equals (friction velocity)^3/(kappa*y).
and k in the log law is (friction-velocity )^2/(sqrt C_mu).

Also, i would not use the standard k-epsilon for these type of flows because of the so-called stagnation point anomaly ( spurious production of k at stagnation region)
davidwilcox is offline   Reply With Quote

Old   April 15, 2016, 05:40
Default
  #3
New Member
 
Join Date: Oct 2015
Location: Oviedo, Asturias, Espaņa
Posts: 17
Rep Power: 10
pela145 is on a distinguished road
davidwilcox,

I will try it in my next simulations and, as soon as get any significant conclusion about it, I will let you know on this thread.

However, in some studies about simulating properly the ABL with CFD, the researchers have used uniform values for k and epsilon. Indeed, there is an inlet boundary condition in openFoam which, based on P.J Richards and R.P Hoxey (1993) logaritmic law, generates a non-uniform inlet U profile while using uniform profiles for both k and epsilon. And that boundary condition is the only one that exist on this programme to create a log law inlet profile, so I thought that it would be fairly correct.

That's precisely what made wonder about all this issue, I found different information from different researchs and, consequently I had no idea what to use. However, I agree with you about the local equilibrium, and I will create two non-uniform vertical profiles for k and epsilon and let's see how does it works.

As an aside, I have already read about the issue related to standard k-epsilon you have mentioned. That is one of the tasks of my project, how and why other turbulence models work more properly than standard kE in that especific point.

Thank you

Pelayo
pela145 is offline   Reply With Quote

Reply

Tags
initial conditions, k epsilon, omega, rans, steady


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
simpleFoam error - "Floating point exception" mbcx4jc2 OpenFOAM Running, Solving & CFD 12 August 4, 2015 02:20
pimpleFoam: turbulence->correct(); is not executed when using residualControl hfs OpenFOAM Running, Solving & CFD 3 October 29, 2013 08:35
calculation stops after few time steps sivakumar OpenFOAM Running, Solving & CFD 7 March 17, 2013 06:37
Orifice Plate with a fully developed flow - Problems with convergence jonmec OpenFOAM Running, Solving & CFD 3 July 28, 2011 05:24
Unknown error sivakumar OpenFOAM Pre-Processing 9 September 9, 2008 12:53


All times are GMT -4. The time now is 06:21.