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vette982
Oct29-09, 09:10 PM
I have the density (ρ) of the particles, the fluid, as well as the complete dimensions of the non-spherical particles. I know the Force of drag (F) and the Coefficient of drag (C). But how do you get the Reynolds number from this? I can't use Stokes' equations because they only apply to spheres.

redargon
Oct30-09, 03:55 AM
So you have non-spherical particles in a flow, or the fluid is made up of non-spherical particles or the object that the flow reacts to is non-spherical? I'm not sure I understand the question, could you rephrase it please?

Andy Resnick
Oct30-09, 08:47 AM
I have the density (ρ) of the particles, the fluid, as well as the complete dimensions of the non-spherical particles. I know the Force of drag (F) and the Coefficient of drag (C). But how do you get the Reynolds number from this? I can't use Stokes' equations because they only apply to spheres.

The Reynolds number has a 'characteristic length' scale

http://en.wikipedia.org/wiki/Reynolds_number

Choice of 'L' depends on the problem. It may refer to the size of an object immersed in flow, or the size of a duct, or some other chacateristic length scale. In your case, I suspect the natural choice is an average diameter.