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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