Kykigi

| stream |Depropanizer feed |Propane prdocut |Debutanizer feed |Butane product |Gasoline product |
| || | | | |
|Component | || | | |


|Mol/hr |Lbmol/hr |Mol % |Mol/hr |Mol % |Mol/hr |Mol % |Mol/hr |Mol % |Mol/hr |Mol % | |C2 |63.17|0.1279 |1.65 |63.17 |3.28 | | | | | | | |C3 |1874.34 |3.79 |48.84 |1837.89 |95.32 |36.45 |1.91 |36.45 |2.94 | | | |IC4 |333.43 |0.68 |8.69 |23.20 |1.20 |310.20 |16.25 |310.20 |25 |0.08 |0.01 | |nC4|877.29 |1.78 |22.86 |3.4 |0.20 |873.48 |45.75 |869.58 |70.08 |3.90 |0.58 | |IC5 |189.63 |0.38 |4.84 | | |185.63 |9.72 |19.89 |1.60 |165.74 |24.80 | |nC5 |294.40 |0.596 |7.67 | | |294.40 |15.42 |4.76 |0.38|289.64 |43.33 | |C6 |156.22 |0.32 |4.07 | | |156.22 |8.18 | | |156.22 |23.37 | |C7 |52.94 |0.11 |1.38 | | |52.84 |2.77 | | |52.84 |7.91 | |TOTAL MOLS/HR |3837.37 | |1928.07 | |1909.30 | |124.88 ||668.42 | | |LBS/HR |207.870 | |84.329 | |123.543 | |71.806 | |51.737 | | |MOL WT |54.15 | |43074 | |64.71 | |57.87 | |77.40 | | |S.G @ 60 °F |0.557 | |0.503 | |0.602 | |0.567 | |0.641 | | |BPSD @60 °F|25.600 | |11.205 | |14.095 | |8557 | |5538 | | |TEMP °F |90 | |119 | |264 | |116 | |105 | | |PRESSURE PSIG |320 | |315 | |275 | |61 | |55 | | |S.G @ TEMP |0.54 | |0.45 | |0.44 | |0.54 | |0.61 | ||GPM @ TEMP |770 | |375 | |562 | |266 | |170 | | |


La alimentación llega en estado liquido a 350 psig y 90 °f

Despropanizadora : 40 etapas feed 20 temperatura de tope 130 f de fondo 248 ypresion 275 psig
Desbutanizadora 34 etapas feed 16 temperatura de tope 131 f fondo 223 f y presion 80 psig

1 mol: 0.00202462 lbmol
1000 mol: 2.02462 lbmol




C-301 119F 265 PSIG
C-302...