| Thread Closed |
Drag Coefficient |
Share Thread | Thread Tools |
| Apr14-09, 11:01 AM | #1 |
|
|
Drag Coefficient
Hi
In a Drag problem, I'm trying to calculate the drag force but I dont know the drag coefficient? Is there any way to calculate it? Thanks |
| Apr14-09, 11:05 AM | #2 |
|
Recognitions:
|
For simple shapes yes (although you can look them up in a table http://en.wikipedia.org/wiki/Drag_coefficient)
Generally for real shapes you have to measure it, either in a wind tunnel or a computer simulation (CFD) |
| Apr14-09, 11:44 AM | #3 |
|
|
Ok, im trying to do a tutorial sheet on it, how do I calculate it say for sphere?
thanks |
| Apr14-09, 12:02 PM | #4 |
|
Recognitions:
|
Drag Coefficient
If you click the link there is a table that lists the Drag Coefficient for a sphere as [tex] C_d = 0.47[/tex]
|
| Apr14-09, 12:53 PM | #5 |
|
|
Yea I have used that but it doesnt give me the required answer.
|
| Apr14-09, 01:45 PM | #6 |
|
Recognitions:
|
Do you mean how do you calculate that it is 0.47 for a sphere, or how do you calculate the drag for a sphere in given conditions?
The drag equation ( propertional Area * velocity^2) is an approximation for high Reynolds number flow (eg air) it isn't necessarily correct for low speed or high viscosity cases. |
| Apr14-09, 02:22 PM | #7 |
|
|
Using the Drag force equation I am trying the force on a sphere as it moves through an oil. The only unknown that I have is the drag coefficient? And if I use 0.47, it doesnt give me the right answer.
Thanks |
| Apr14-09, 02:56 PM | #8 |
|
Recognitions:
|
[tex] C_f = \frac{24}{R^*} \left( 1 + \frac{3}{16}R^* - \frac{7k}{48}R^* \right)\,\,R^*=2R [/tex] Not sure why it's written like that, but oh well. [tex]R\equiv [/tex] Reynolds number of course. [tex] k = V^* / U_\infty[/tex] where V* is the radial velocity of blowing through the surface...which I assume you can take to be zero in your case. There is also a "famous" Oseen's (1910) drag coefficient forumula for a sphere in uniform stream: [tex] C_D = \frac{24}{{Re}_D}\left(1+\frac{3}{16}{Re}_D\right)[/tex] Stokes gave an exact solution in the limit as Re->0, such as creeping flow, where: [tex] C_D = \frac{24}{{Re}_D}[/tex] However, that's only valid where Reynolds is less than 0.2. What type of Reynolds are you looking at? |
| Apr14-09, 03:16 PM | #9 |
|
|
Well I calculate my Reynolds number to be 9.9, the velocity of the sphere is 0.08m/s, the density is 850, diameter of the sphere is 14.7(10)^-3, and the viscosity is 0.1 which yields 9.996?
Also from the drag equation, where I use area, will it be the surface area of the sphere, i.e. d^2*pi. Thanks |
| Apr14-09, 04:07 PM | #10 |
|
|
|
| Thread Closed |
| Thread Tools | |
Similar Threads for: Drag Coefficient
|
||||
| Thread | Forum | Replies | ||
| Drag Coefficient out by a factor of 10, can anyone help?? | General Physics | 1 | ||
| Fluid Mechanics - Drag coefficient and Pressure coefficient | Mechanical Engineering | 1 | ||
| Determining Drag Coefficient | Introductory Physics Homework | 6 | ||
| Drag coefficient PVC over water | Mechanical Engineering | 9 | ||
| Coefficient of Drag | General Physics | 2 | ||