Page 191 - Standard Handbook Of Petroleum & Natural Gas Engineering
P. 191
176 General Engineering and Science
Values of (VD) for Water at 60°F (velocity in fps X diameter in inches)
0.1 02 0.4 08 0.81 2 4 6 8 10 20 40 6080100 200 400 600 lp00 2,WO 4000 Spa0 l0.W
0.1
0.09
0.08
0.07
0.06
- 0.05
-? 0.04
2
B
s?
I1 -
> 0.03
0.025
3
'E
s 0.02
c
L
0.015
0.01
0.009
0.008
ReynoldsnumkrR= (Vlnrps dmn. vmtzpersec)
Figure 2-21. Friction factor for flow in pipes [l].
D = 2A/C = 0.0833 ft
v = Q/A = [(1,000 gal/min)(0.1337 fts/ga1)/(60 s/min)]
= .0278 ft' = 80.21 ft/s
= 7,380 x lb-s/ft2 @ 32°F
= 647 x Ib-s/ft' @ 104°F
g = 32.2 ft/s2
At 32°F
(56.60)( 0.0833)( 80.21) = 1, 59
R=
(32.2)(7,380x lod)
Because R < 2,000 the flow is laminar and f = 64/R = 0.04022. Assuming that the fluid is
incompressible implies that yl = y, and v1 = v2, and Equation 2-54 can be rewritten as
(0.04022)( 100)(80.21)' 1
2( 32.2)( 0.0833)
/( 144 in.'/ft2
= 124psi

