Example [HW]; A wet gas produces from a separator at 300 psia and 73 F to a stock tank at 76. The separator produces 69551 scf/STB and stock tank vents 366 scf/STB. The stock tank liquid API is 55.9. Calculate Bwg at 2360 psig and 204 F. Component Composition, Critical Critical mole fraction temperature, pressure, 10.869 R psia Yi Tal Paj 0.82280 342.91 666.4 C₂ 0.0952 549.50 706.5 Ca 0.0464 0.0 665.64 616.0 i- C4 0.0064 734.04 527.0 n-C4 0.0096 765.20 550.6 1- C5 0.0035 828.68 490.4 n-C5 0.0029 845.38 488.6 Ce 0.0029 913.18 436.9
Example [HW]; A wet gas produces from a separator at 300 psia and 73 F to a stock tank at 76. The separator produces 69551 scf/STB and stock tank vents 366 scf/STB. The stock tank liquid API is 55.9. Calculate Bwg at 2360 psig and 204 F. Component Composition, Critical Critical mole fraction temperature, pressure, 10.869 R psia Yi Tal Paj 0.82280 342.91 666.4 C₂ 0.0952 549.50 706.5 Ca 0.0464 0.0 665.64 616.0 i- C4 0.0064 734.04 527.0 n-C4 0.0096 765.20 550.6 1- C5 0.0035 828.68 490.4 n-C5 0.0029 845.38 488.6 Ce 0.0029 913.18 436.9
Chapter2: Loads On Structures
Section: Chapter Questions
Problem 1P
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![Example [HW]; A wet gas produces from a separator at 300 psia and 73 F to a stock
tank at 76. The separator produces 69551 scf/STB and stock tank vents 366 scf/STB. The
stock tank liquid API is 55.9. Calculate Bwg at 2360 psig and 204 F.
Component Composition,
Critical
Critical
mole fraction temperature, pressure,
10.869
R
psia
Yi
Tal
Paj
0.82280
342.91
666.4
C₂
0.0952
549.50
706.5
Ca
0.0464
0.0
665.64
616.0
i- C4
0.0064
734.04
527.0
n-C4
0.0096
765.20
550.6
1- C5
0.0035
828.68
490.4
n-C5
0.0029
845.38
488.6
Ce
0.0029
913.18
436.9](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Fd3041687-8ecc-4d3e-a323-3d11a576ec95%2Fc8c18b6a-4475-401f-a181-2b0cf2ef19d5%2Fp08qd7k_processed.jpeg&w=3840&q=75)
Transcribed Image Text:Example [HW]; A wet gas produces from a separator at 300 psia and 73 F to a stock
tank at 76. The separator produces 69551 scf/STB and stock tank vents 366 scf/STB. The
stock tank liquid API is 55.9. Calculate Bwg at 2360 psig and 204 F.
Component Composition,
Critical
Critical
mole fraction temperature, pressure,
10.869
R
psia
Yi
Tal
Paj
0.82280
342.91
666.4
C₂
0.0952
549.50
706.5
Ca
0.0464
0.0
665.64
616.0
i- C4
0.0064
734.04
527.0
n-C4
0.0096
765.20
550.6
1- C5
0.0035
828.68
490.4
n-C5
0.0029
845.38
488.6
Ce
0.0029
913.18
436.9
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