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

y+ values

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   July 28, 2004, 13:08
Default y+ values
  #1
julie
Guest
 
Posts: n/a
Hi everyone,

I am modelling a flow in a penstock with a reynolds number of 2x10^7. I use k-epsilon model in Fluent.

First, I ran the case with a very fine mesh and had an error like : "turbulent viscosity ratio limited to ... in ... cells". Hence I used another model (rng and k-omega) but it did not solve the problem. Reading the Fluent documentation and messages on this site I went to the idea that the problem may come from the y+ values and the density of the mesh. I checked my y+ values and effectively I saw they were all under 30.

Then I have done a coarser mesh and the problem of turbulent viscosity disapeared. However the y+ values are still below 30. Once again I changed the turbulence model but no better results.

Besides, the velocity contours I obtain are all very different depending if I use the k-epsilon, the RNG or the k-omega model and also when I change the mesh size.

Any comments are welcome.

Regards,

Julie
  Reply With Quote

Old   July 28, 2004, 15:37
Default Re: y+ values
  #2
Charles
Guest
 
Posts: n/a
You want low Y+ values. These will vary on what boundary conditions you are using. The velocities will be different for different turbulence models. Usually the best one depends on your application and also if you have experimental data to compare them to.
  Reply With Quote

Old   July 28, 2004, 15:50
Default Re: y+ values
  #3
julie
Guest
 
Posts: n/a
Hi Charles,

I thought y+ value should be between 30 and 50 to provide accurate results in the boundary layer.

As boundary conditions, I used a velocity inlet with a 3m/s velocity, 5% turbulent intensity (but this is just an asumption) and a hydraulic diameter of 4574mm. But why do you say boundary conditions can influence the y+ values?

Besides I have experimental data but when I compare the results they are totally different. The range of velocities is the same but the profile is very different.

Any idea?

  Reply With Quote

Old   July 28, 2004, 16:18
Default Re: y+ values
  #4
Charles
Guest
 
Posts: n/a
Yes, Y + should be > 30 to 60. At Y+<11.225 Fluent employs the linear(laminar) law. So using a excessively fine mesh near the wall should be avoided because the wall functions cease to be valid in the viscous sublayer. You said your Y+ was below 30, correct? Fluid properties affect Y+ such as density, viscosity, and friction velocity. This is stated in the Fluent manual. Also, as Reynolds number increases the upper bound of Y+ increases. What wall functions were you using for each turbulence model?
  Reply With Quote

Old   July 28, 2004, 16:21
Default Re: y+ values
  #5
julie
Guest
 
Posts: n/a
I used the standard wall functions, i.e. the default ones.
  Reply With Quote

Old   July 29, 2004, 03:17
Default Re: y+ values
  #6
laika
Guest
 
Posts: n/a
be carefull with statements of y+

If you use standard k-eps, y+ must indeed be >30 and somewhat below 50.

But if you use k-omega, y+ values should be very low (around 3) to have good results.

Julie, you have a very high Re. Is your flow swirling? How big is the geometry?

Julie, you state the results depend on mesh size. That looks like an insufficient mesh-resolution...

kind regards,

Laika, still orbiting
  Reply With Quote

Old   July 29, 2004, 10:20
Default Re: y+ values
  #7
julie
Guest
 
Posts: n/a
Thank you for your help, but what can I do to obtain higher y+ values with the k-epsilon model?

How can I know if swirling. i do not have this info from the experiements.

Concerning the geometry, the pipeline is almost 43m long with a diameter of 3.92m.

regards

julie
  Reply With Quote

Old   November 29, 2009, 16:24
Default
  #8
New Member
 
Join Date: Oct 2009
Posts: 24
Rep Power: 16
doodek is on a distinguished road
Hello,
I have a question. Which should be y+ when i'm using k-omega SST model?
A few posts previously laika said that "around 3", but there:
http://www.cfd-online.com/Wiki/Near-...k-omega_models
is an information, that y+ should be around 30 (if i don't use transitional flows option). What is truth?

Best regards,
doodek
doodek is offline   Reply With Quote

Old   November 30, 2009, 04:54
Default
  #9
Senior Member
 
Philipov's Avatar
 
Svetlin Filipov
Join Date: Mar 2009
Location: United Kingdom
Posts: 176
Rep Power: 17
Philipov is on a distinguished road
Try to compute turbulent intensity... not guess! There is an easy formula for internal and external flows... use it.
Advice: use Wiki.. but read manual and consult providers!
Philipov is offline   Reply With Quote

Old   November 30, 2009, 07:04
Default
  #10
New Member
 
Join Date: Oct 2009
Posts: 24
Rep Power: 16
doodek is on a distinguished road
I know only empirical correlation for pipe flows. Which are other formulas? In my case I have flows between a few rows of pipes, so I guess that I should set up value of turbulence intensity.
doodek is offline   Reply With Quote

Old   November 30, 2009, 07:54
Default
  #11
Senior Member
 
Philipov's Avatar
 
Svetlin Filipov
Join Date: Mar 2009
Location: United Kingdom
Posts: 176
Rep Power: 17
Philipov is on a distinguished road
7.2 Flow Inlet and Exit Boundary Conditions
Uniform Specification of Turbulence Quantities
Fluent UG.. the formula is described
Philipov is offline   Reply With Quote

Old   December 1, 2009, 03:44
Default
  #12
Senior Member
 
karine
Join Date: Nov 2009
Posts: 158
Rep Power: 16
thecfduser is on a distinguished road
U can use y+>30 without transitional flow or y+=1 with trans flow. U will get a near result if ure boundary layer is not subjected to severe adverse pressure gradients....
However it is better to use a y+=1 since the k-w is essentially a low Re....

With k-epsilon, using a y+>30 and law of the wallis usually better than y+=1 with enhanced treatement
thecfduser 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
TimeVaryingMappedFixedValue irishdave OpenFOAM Running, Solving & CFD 32 June 16, 2021 06:55
Ensight - node values -cell values leo FLUENT 1 May 12, 2010 08:47
max node values exceed max element values in contour plot jason_t FLUENT 0 August 19, 2009 11:32
exact face values RubenG Main CFD Forum 0 June 22, 2009 11:09
strange node values @ solid/fluid interface - help JB FLUENT 2 November 1, 2008 12:04


All times are GMT -4. The time now is 09:48.