Expt SEPS4 : 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 0.3959 Cumulative vapour mole fraction 0.6041 Cumulative Surface volume oil M3 0.0954 Cumulative Surface volume gas SM3 14.5311 Cumulative GOR (Calculated) SM3/M3 152.3488 Cumulative GOR (Observed ) SM3/M3 160.0000 Oil FVF (from Phig) (Calculated) RM3/SM3 1.4012 Oil FVF (from Phig) (Observed ) RM3/SM3 1.4000 ------------------- ------------ ------------ Liquid Vapour Fluid properties ------------ ------------ Calculated Calculated ------------------- ------------ ------------ Mole Weight 200.1843 21.1317 Z-factor 0.0100 0.9962 Viscosity 1.7726 0.0105 Density KG/M3 830.9981 0.8818 Molar Vol M3/KG-ML 0.2409 23.9641 ------------------- ------------ ------------ ------------------- ------------ ------------ ------------ ------------ Molar Distributions Total, Z Liquid,X Vapour,Y K-Values Components ------------ ------------ ------------ ------------ Mnemonic Number Measured Calculated Calculated Calculated ------------------- ------------ ------------ ------------ ------------ CO2 1 0.6409 0.0132 1.0522 79.4653 N2 2 0.0294 3.3078E-06 0.0486 14699.0310 C1 3 49.0529 0.1252 81.1235 647.8344 C2 4 4.9846 0.3631 8.0139 22.0734 C3 5 4.0519 1.7850 5.5377 3.1024 IC4 6 1.3484 1.4500 1.2817 0.8839 NC4 7 2.1885 2.9776 1.6712 0.5612 IC5 8 1.0480 2.0046 0.4210 0.2100 NC5 9 1.1449 2.3413 0.3607 0.1540 F1 10 1.4631 3.3220 0.2447 0.0737 F2 11 6.8586 17.0044 0.2083 0.0122 F3 12 7.9710 20.0777 0.0355 0.0018 F4 13 4.9215 12.4284 0.0009 7.2436E-05 F5 14 5.1346 12.9680 2.2700E-05 1.7505E-06 F6 15 9.1618 23.1394 3.4457E-13 1.4891E-14 ------------------- ------------ ------------ ------------ ------------ Composition Total 100.0000 100.0000 100.0000 ------------------- ------------ ------------ ------------ ------------