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October 4, 2002, 16:05 
drag coefficient

#1 
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( drag coefficient ) / (density * Uinfin. *Uinfin.) is very close to the experimental data. Is it possible that Fluent has a bug in the drag coefficient calculation? Thanks. 

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October 7, 2002, 09:03 
Re: drag coefficient

#2 
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The drag coefficient is calculated using the values in: report > reference values So its possible that your reference area is set wrong.


October 7, 2002, 13:33 
Re: drag coefficient

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Dear Glenn:
Your message is not clear for me. I didn't set the reference area. I got the drag coefficient from: Solve  > Monitors  > Force  > drag coefficient and that value matches with Report  > Forces  > total coefficient for vector (1,0,0). Thanks,  Jean 

October 7, 2002, 14:25 
Re: drag coefficient

#4 
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Hi Glenn,
I understand what you mean now. In Report > Referance Values, the Area = 1 m^2 and it should be Pi*D^2. Since D=1, so it will be Cd_new=Cd/Pi. The value is still not right! Thanks,  Jean 

October 8, 2002, 03:19 
Re: drag coefficient

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Guys, Sorry to interject, but I have a converged flow field with no objects in it and was wondering if I can report the drag coefficient on an imaginary sphere where I would set its properties (i.e. density, diameter)?
Rex 

October 8, 2002, 05:48 
Re: drag coefficient

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Im not too sure about this, but I think that you can only calculate the drag on a 'wall' boundary condition. However maybe someone knows different????


October 9, 2002, 19:00 
Re: drag coefficient

#7 
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Rex, what do you mean by an imaginary sphere? How do you model a sphere as being imaginary?


October 10, 2002, 03:12 
Re: drag coefficient

#8 
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I mean that if there was a sphere in the flow field (there isn't one really), could you report, for instance, the drag force being experienced at that point?
Rex 

October 11, 2002, 20:23 
Re: drag coefficient

#9 
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If you imagine its there, then the model will not realize it and it wont give you anything. But if you incorporate it in your model, you can set the reference values, and monitor the drag coefficient.
Your answer is yes. Report>reference values: set the frontal area, the velocity, density, etc Solve>monitors>force: select drag and the sphere wall 

October 30, 2002, 05:39 
Re: drag coefficient

#10 
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Hey Rex, surely the flow would be perturbed by the sphere, so changing its characteristics and hence the Drag ? unless you can some how take into account the effect the sphere has upon the flow ? I guess though if the shere were very small then its influence on the flow would be negligable, but then so would its drag ??? What is the interest of calculating the drag this way round ?? bob


October 30, 2002, 08:50 
Re: drag coefficient

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That's an interesting study.
What's is the status of your project? For who are you doing this? For wich values of Re are you calculating? How is your mesh? are you willing to share some results with us? greetings, Laika, still orbiting 

October 30, 2002, 09:48 
Re: drag coefficient

#12 
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The so called mechanistic models for particulate transport I am using in conjunction with Fluent flow data assume that the spheres do not effect the characteristices of the flow field (velocity profile, etc.), so how the particles modify the flow is not an issue I'm looking at. I just want to know the forces being experienced over a certain (predefined by me) area are.


October 31, 2002, 15:51 
Re: drag coefficient

#13 
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Dear Glenn,
As you have mentioned that the drag coefficient is calculated using the values in: report > reference values. I have found that in my case, the problem is not reference area but reference velocity. For both pressure coefficient and drag coefficient, correction should be made by divided (V_inf * V_inf). Many thanks,  Jean 

October 31, 2002, 15:55 
Re: drag coefficient

#14 
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Hi Laika,
Thanks for the email. I am willing to share some my results with you. I will email you later.  Jean 

November 4, 2002, 04:49 
Re: drag coefficient

#15 
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thanks!!
Laika, still orbiting 

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