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March 14, 2011, 17:46 

#41  
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Joshua Counsil
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Quote:
Observing the graph, the kw SST model provides the worst result, with the kw SSTtrans providing slightly better, though still poor, results. The gammatheta provides much better results, so my above assumption makes sense. 

March 15, 2011, 17:00 

#42  
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Martin Hegedus
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In my opinion, at these Reynolds number the concept of turbulence takes on a different meaning than at higher Reynolds numbers. At these Re numbers the turbulent eddies are largish in scale. They are more macro than micro. The SA turbulence model is just picking up on the vorticity in the problem and creating eddy viscosity. The eddy viscosity then dampens out the problem and provides steadiness. As the Re number increases, micro unsteadiness builds up on the bubble facilitating the bubble's reattachment and the macro unsteadiness goes away, leaving only micro turbulence. At this point I guess turbulence models become more relevant. Or, another way of viewing reattachment is that by going from Re 5,0000 to 50,000 one has given more surface length (10 times) for the bubble to reattach itself. Thus, macro and micro are relative. Maybe the eddies actually remain sort of on the same real scale as the airfoil is stretched to 10 X, but relative to the airfoil length they are 10 times smaller? 

March 15, 2011, 17:52 

#43  
Senior Member

Quote:
It is interesteresting at this reynolds numbers the turbulence is indeed "macroscopic" in a sence that Kolmogorov lenght Re^3/4 is of orer of 10^3 which is .1% of the wing chord. 

March 15, 2011, 18:09 

#44 
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Martin Hegedus
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I do agree that the flow is unsteady. Unfortunately I'm running these on my laptop which doesn't have the horse power to adequately model the unsteady flow.


March 15, 2011, 18:23 

#45 
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Joshua Counsil
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Chances are the flow is laminar and unsteady and that while laminar separation occurs, neither transition nor reattachment do. Like you said, the eddy viscosity dampens the effect.


March 17, 2011, 14:36 

#46 
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Raashid Baig
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Hi,
I will like to take forum's attention to a very similar problem that I faced while trying to simulate wind turbine NREL phase VI simulations. It's a low speed flow problem where the Reynolds numbers are around 1e06 or below. Experimental results are available for the base aerofoil S809 (See the attached images). These experimental oil flow lines show that they have all the problems associated with low speed laminar flows (Laminar separation, bubble formation and turbulent reattachment). But just today I found a paper by Dr Menter  "Predicting 2D Airfoil and 3D Wind Turbine Rotor Performance using a Transition Model for General CFD Codes", R. Langtry, J. Gola and F. Menter, ANSYS CFX, Otterfing, Germany, AIAA20060395 44th AIAA Aerospace Sciences Meeting and Exhibit It uses the SST Transitional model and surprisingly these are the most consistent set of results that I have seen for this set of experiments. The results may not be very accurate but they manage to give consistency and are always around 10% of the experimental values. Please let me know your thoughts on the same and are there any other methods which can give more accurate and consistent results ??????????? 

March 17, 2011, 16:28 

#47 
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March 16, 2012, 01:10 
Flow over stepped airfoil

#48  
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I've been reading some of your post and found out that you've worked on flow over stepped airfoils. I've also been working on stepped model airfoils for the past 3 weeks but with no luck. Now the problem is I'm stuck up in selecting a viscous model in Fluent. The problem description is as follows: airfoil chord: 0.25 m Reynolds number: 67000 domain: cgrid; 10c semicircle, 20c chordwise, 10c total height. I'm using Low Re airfoils namely Eppler 61 and NACA 4415. I've tried SA, KE and all but the results are not matching with WT results. I doubt that the flow over the airfoil would be either laminar or fully turbulent. it sure must be in the transition region. Although I've not used any transition model and I dont know what parameters for the transition model to set. The problem is, the solution converges but doesn't give the correct values (doesn't match with published results). This is only about normal airfoils. Second step would to be make a step and run the simulation again. I hope you will share some of your experiences in solving this problem. TIA Hemant 

March 16, 2012, 03:56 

#49 
Senior Member

Hi Hemant,
I have tried different turbulence models without much success: It sems that only LES should give something more or less close to reality. I have also tried the following thing with stepped airfoils: At low angles of attack and in the case when the step is close enough to the leading edge, transition will happen at the step. So, I have written a user defined function which switches the turbulence model on over top surface of the foil at the step location. At the bottom surface the model is switched on at the trailing edge (see image attached). Truffaldino 

March 19, 2012, 18:09 

#50 
New Member

hello for everybody
i'm just biginner in cfd and i want specially to ask Martin Hegedus , why u used turbulence model and u r sur that the flux around airfoil is still laminar [Re=70000<5e5] , it's not clear for me , can you explan me please thank you 

March 19, 2012, 18:11 

#51 
New Member

hello for everybody
i'm just biginner in cfd and i want specially to ask Martin Hegedus , why u used turbulence model and u r sur that the flux around airfoil is still laminar [Re=70000<5e5] , it's not clear for me , can you explan me please thank you 

March 19, 2012, 19:57 

#52 
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Martin Hegedus
Join Date: Feb 2011
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Yikes, this thread is almost a year old. I did quickly scan it, but can't say I remember all the details.
At 70,000 I don't think a RANS model is appropriate, but it goes give you insights into what the flow is doing. Also, since SA tends to be on the stable side, it gets you steady state solutions. Less expensive than time accurate. As the Re for a RANS model decreases, so does the eddy viscosity. As the eddy viscosity decreases the RANS solution becomes more like a laminar one. The RANS solution is only "turbulent" once the eddy viscosity has had a chance to build up. As the Re drops, I believe, the skin friction drag for RANS approaches laminar. This is true only if there isn't separation of one sort or another (flat plate is an example). However, separation is a different issue. Even for low Res, a RANS model has enough eddy viscosity to dampen out or greatly affect the unsteadiness so it will not behave like a laminar result. One thing that can be done with a RANS model is to limit the amount of eddy viscosity to see what it takes to make the solution go unsteady. This can give you an idea of how appropriate the RANS model is. 

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