Expt SEPS3 : Separators Peng-Robinson (3-Parm) on ZINIT with PR corr. Lohrenz-Bray-Clark Viscosity Correlation ----------------------------------------------------------------------- Cumulatives for Separator Train ----------------------------------------------------------------------- Standard pressure BARSA 1.0132 Standard temperature Deg C 20.0000 Cumulative liquid mole fraction 0.3663 Cumulative vapour mole fraction 0.6337 Cumulative Surface volume oil M3 0.0925 Cumulative Surface volume gas SM3 15.2441 Cumulative GOR (Calculated) SM3/M3 164.8771 Cumulative GOR (Observed ) SM3/M3 129.2400 Oil FVF (from Phig) (Calculated) RM3/SM3 1.4455 Oil FVF (from Phig) (Observed ) RM3/SM3 1.3480 ------------------- ------------ ------------ Liquid Vapour Fluid properties ------------ ------------ Calculated Calculated ------------------- ------------ ------------ Mole Weight 210.6144 23.4768 Z-factor 0.0105 0.9954 Viscosity 1.8186 0.0103 Density KG/M3 834.4265 0.9804 Molar Vol M3/KG-ML 0.2524 23.9449 ------------------- ------------ ------------ ------------------- ------------ ------------ ------------ ------------ Molar Distributions Total, Z Liquid,X Vapour,Y K-Values Components ------------ ------------ ------------ ------------ Mnemonic Number Measured Calculated Calculated Calculated ------------------- ------------ ------------ ------------ ------------ CO2 1 0.6409 0.0144 1.0030 69.6253 N2 2 0.0294 5.2949E-05 0.0463 874.7894 C1 3 49.0529 0.3635 77.1975 212.3714 C2 4 4.9846 0.2308 7.7326 33.5083 C3 5 4.0519 0.6728 6.0051 8.9251 IC4 6 1.3484 0.5625 1.8027 3.2050 NC4 7 2.1885 1.2760 2.7159 2.1285 IC5 8 1.0480 1.1751 0.9746 0.8293 NC5 9 1.1449 1.5257 0.9247 0.6061 F1 10 1.4631 2.6924 0.7526 0.2795 F2 11 6.8586 17.4600 0.7305 0.0418 F3 12 7.9710 21.5663 0.1124 0.0052 F4 13 4.9215 13.4317 0.0022 0.0002 F5 14 5.1346 14.0172 3.8983E-05 2.7811E-06 F6 15 9.1618 25.0116 7.7817E-14 3.1112E-15 ------------------- ------------ ------------ ------------ ------------ Composition Total 100.0000 100.0000 100.0000 ------------------- ------------ ------------ ------------ ------------