Dear Friends,
Could anybody tell me why the Moody chart from TP 410 ed. 2009 is different from 1999 ed.?
Thank You
Dear Friends,
Could anybody tell me why the Moody chart from TP 410 ed. 2009 is different from 1999 ed.?
Thank You
Go here for a discussion
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Perry's pipe friction loss equation has a 4 coefficient, and the chart is 4 time less than Crane # 410. Now Crane #410's chart is 400% larger, but their friction loss equation drops the 4 coefficient. Therefore, both ways produce the same numbers in the end.
The graphs in Crane #410 (A-24 and A-25) are for Moody Friction factor, which is 4 times Fanning friction factor. That is, f = 64/Re is Moody and f = 16/Re is Fanning.
Be careful. It is easy to mix the two and calculate 400% greater (or 25% less) head loss. The calculation for head loss in feet is:
using Moody Friction factor -
h(friction) = f(M) * (L/D) * v^2 / (2 * g)
using Fanning Friction factor -
h(friction) = 4*f(F) * (L/D) * v^2 / (2 * g)
where,
f(M) = Moody Friction factor
f(F) = Fanning Friction factor
L = length in feet
D = pipe inside diameter in feet
v = velocity in ft/s
g = 32.174 ft/s^2, acceleration due to gravity
The Colebrook-White equation is an iterative method that calculates Fanning friction factor.
f(F)^2 = 1 / ( -4 * Log(eps / (3.7 * D) + 1.256 / (Re * √f(F) )
where,
eps = pipe roughness in feet
Re = Reynold's number
Thank You.
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