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Unread 05-01-2003, 04:50 PM   #41
bigben2k
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Join Date: May 2002
Location: Texas, U.S.A.
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Quote:
Originally posted by bigben2k
Now if I could apply Since87's equation, I could draft up my own curve...
Given the numbers, and using dP=Q^2 * Rf, where
dP = Pressure drop
Q=flow
Rf = {flow resistance}

and

dP = 0.12 psi @ 0.5 gpm
dP = 0.25 psi @ 5.0 gpm

I get 0.48 and 0.01 for Rf, respectively.:shrug:
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