Celia operadores

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Case Name: universidad tecnologica de altamira altamira,tamaulipas Unit Set: Date/Time:

C:\USERS\TOÑA\DESKTOP\REPORTE INFO 3.HSC NewUser Mon Feb 28 16:09:20 2011 Fluid Package: Property Package:Basis-1 NRTL - Ideal

Material Stream: 1
CONDITIONS
Overall Vapour / Phase Fraction Temperature: Pressure: Molar Flow Mass Flow Std Ideal Liq Vol Flow Molar Enthalpy Molar Entropy Heat Flow Liq Vol Flow @Std Cond (C) (kPa) (lbmole/hr) (kg/h) (barrel/day) (Btu/lbmole) (Btu/lbmole-F) (Btu/hr) (barrel/day) 0.2156 90.00 * 130.0 * 15.86 255.0 * 40.93 -8.819e+004 8.556 -1.399e+006 39.15 * VapourPhase 0.2156 90.00 130.0 3.420 83.45 13.35 -4.792e+004 28.24 -1.639e+005 12.96 Liquid Phase 0.1289 90.00 130.0 2.045 86.40 14.70 7683 -7.009 1.572e+004 14.63

Aqueous Phase 0.6555 90.00 130.0 10.40 85.15 12.88 -1.203e+005 5.141 -1.251e+006 12.67

PROPERTIES
Overall Molecular Weight Molar Density Mass Density Act. Volume Flow Mass Enthalpy Mass Entropy Heat Capacity Mass Heat Capacity LowerHeating Value Mass Lower Heating Value Phase Fraction [Vol. Basis] Phase Fraction [Mass Basis] Partial Pressure of CO2 Cost Based on Flow Act. Gas Flow Avg. Liq. Density Specific Heat Std. Gas Flow Std. Ideal Liq. Mass Density Act. Liq. Flow Z Factor Watson K User Property Partial Pressure of H2S Cp/(Cp - R) Cp/Cv Heat of Vap. Kinematic Viscosity Liq. Mass Density (Std. Cond) Liq. Vol. Flow (Std. Cond)Liquid Fraction Molar Volume Mass Heat of Vap. Phase Fraction [Molar Basis] Surface Tension Thermal Conductivity Viscosity Cv (Semi-Ideal) Mass Cv (Semi-Ideal) Cv Mass Cv Cv (Ent. Method) Mass Cv (Ent. Method) Cp/Cv (Ent. Method) (dyne/cm) (Btu/hr-ft-F) (cP) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (ft3/lbmole) (Btu/lb) (Btu/lbmole) (cSt) (lb/ft3) (barrel/day)(kPa) (kPa) (Cost/s) (ACFM) (lbmole/ft3) (Btu/lbmole-F) (MMSCFD) (lb/ft3) (USGPM) (lbmole/ft3) (lb/ft3) (barrel/day) (Btu/lb) (Btu/lb-F) (Btu/lbmole-F) (Btu/lb-F) (Btu/lbmole) (Btu/lb) 35.44 1.240e-002 0.4394 5469 -2489 0.2414 21.04 0.5936 3.423e+005 9660 0.3261 0.3272 0.0000 0.0000 --1.657 21.04 0.1442 58.72 0.8572 --9.700 --0.0000 1.104 1.021 1.722e+004 --61.38 39.15 0.7844 80.65 486.0 0.2156------19.05 0.5376 20.61 0.5815 ------Vapour Phase 53.78 2.688e-003 0.1446 5440 -890.9 0.5251 17.99 0.3345 6.508e+005 1.210e+004 0.3261 0.3272 --0.0000 21.21 1.096 17.99 3.109e-002 58.92 --1.000 9.412 ----1.124 1.124 --4.071 60.68 12.96 0.0000 372.0 --0.2156 --1.024e-002 9.428e-003 16.00 0.2975 16.00 0.2975 ------Liquid Phase 93.13 0.5483 51.06 15.95 82.50 -7.526e-002 41.32 0.4436 1.563e+0061.678e+004 0.3591 0.3388 --0.0000 --0.5949 41.32 1.859e-002 55.40 0.4651 4.902e-003 9.927 ----1.050 1.221 --0.3525 55.66 14.63 1.000 1.824 --0.1289 20.50 6.859e-002 0.2883 39.33 0.4223 33.83 0.3632 ------Aqueous Phase 18.05 3.306 59.69 13.44 -6664 0.2848 18.05 0.9999 808.2 44.77 0.3148 0.3339 --0.0000 --3.450 18.05 9.452e-002 62.28 0.3921 8.129e-004 10.08 ----1.124 1.182 --0.3256 63.35 12.67 1.0000.3025 --0.6555 60.47 0.3905 0.3113 16.06 0.8898 15.27 0.8457 -------

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Case Name:universidad tecnologica de altamira altamira,tamaulipas Unit Set: Date/Time:

C:\USERS\TOÑA\DESKTOP\REPORTE INFO 3.HSC NewUser Mon Feb 28 16:09:20 2011 Fluid Package: Property Package: Basis-1 NRTL - Ideal

Material Stream: 1 (continued)
PROPERTIES
Overall Reid VP at 37.8 C True VP at 37.8 C (kPa) (kPa) 9.398 16.00 40.25 Vapour Phase 11.02 17.66 12.96 Liquid Phase --14.75 14.63

Aqueous...