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 Reference : API RP 14 E DATA P1, upstream pressure 550 psig 564.7 S, spesic Grait! 0.7" #, $%mpressi&i'it! (act%r 0.)6)6 *g, gas +% rate 70  -1, gas in'et temperature )5 545 , engt/ %f Pipe 14)50 m 100 16 2a'' -/ic3ness 0.75 I 15."5 E 0.5 PRESSURE DROP CALCULATION Metode Weymouth A 1,60".0 0.001065 $ 65.0) P", %nstream pressure 564.64 psia  54.4 psig Pressure r%p 0.06 psi8100 ft OK S!arat 9a 1 psi8100 ft GAS VELOCITY CALCULATION Gas ; e'%cit! 15.14 ft8s OK S!arat 10 < 60 0.07 0.076"717 % (

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Sizing Pipeline diameter with required pressure drop and allowable velocity

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Sheet1Reference :API RP 14 EDATAP1, upstream pressure550psig564.7psiaS, spesific Gravity0.72Z, Compressibility Factor0.8686Qg, gas flow rate 70MMSCFDT1, gas inlet temperature85oF545oRL, Length of Pipe14850m100ftOD16inWall Thickness0.375inID15.25inE0.95

PRESSURE DROP CALCULATIONMetode WeymouthMetode PanhandleA1,602.0A6.86B0.0019093659B45.0014648899C65.08P2, downstream pressure564.66P2, downstream pressure564.64psia549.96psig549.94psigPressure drop0.04psi/100 ftOKPressure drop0.06psi/100 ftOK

SyaratMax1psi/100 ft

GAS VELOCITY CALCULATIONGas Velocity15.14ft/sOK

Syarat10-60ft/s0.070.0762716625

Sheet2

Sheet3


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