Page 541 - Standard Handbook Petroleum Natural Gas Engineering VOLUME2
P. 541
Flow of Fluids 495
pbrr = 14.7 psia
T, = 75°F
Tp = 105'F
S.G.p = 0.752
S.G., = 54"API
Q, = 480 bpd (std) q,,, = 0 bpd (std)
4L=9,+90
pg = 0.020 cp (constant value)
a, = 28 dyn/cm
GLR = GOR = 3393 scf/bbl
Choose a commercial steel pipe.
Solutions
1. Determine the specific gravity of the oil:
SG, = 141.5 - - 141e5 -0.763
131.5 + API 131.5 + 54
2. Find the weight associated with 1 bbl of stock-tank liquid
m = SG,(350)( l+$0R)+SG0(350)( 1 + WoR WOR )+(0.0764)(GLR)(!3Gg)
1 1
= 0.763(350)(%) + 0.763(S50)(lco) +0.0764(3393)(0.752)
= 462 IWstb of oil
3. Determine the specific weight of the liquid phase:
1 WOR
yL = 6n'4~0( + WOR)'sGw( 1 + WOR)]
1
= 47.6 Idft5

