Phase Fraction [Vol. Basis] 1.000
Phase Fraction [Mass Basis] 2.122e-314 0.0000 1.000
Partial Pressure of CO2 (kPa) 0.0000
Cost Based on Flow (Cost/s) 0.0000 0.0000 0.0000
Act. Gas Flow (ACT_m3/h)
Avg. Liq. Density (kgmole/m3) 8.626 8.646 8.626
Specific Heat (kJ/kgmole-C) 209.6 157.9 209.6
Std. Gas Flow (STD_m3/h) 4.820e+004 0.0000 4.820e+004
Std. Ideal Liq. Mass Density (kg/m3) 627.0 626.0 627.0
Act. Liq. Flow (m3/s) 7.909e-002 7.909e-002
Z Factor 0.8168 3.479e-002
Watson K 13.03 13.04 13.03
User Property
Partial Pressure of H2S (kPa) 0.0000
Heat of Vap. (kJ/kgmole) 2.023e+004
Kinematic Viscosity (cSt) 0.2053 0.4108 0.2053
Liq. Mass Density (Std. Cond) (kg/m3) 629.7 628.7 629.7
Liq. Vol. Flow (Std. Cond) (m3/h) 235.3 0.0000 235.3
Liquid Fraction 1.000 0.0000 1.000
Molar Volume (m3/kgmole) 0.1397 3.280 0.1397
Mass Heat of Vap. (kJ/kg) 278.3
Phase Fraction [Molar Basis] 0.0000 0.0000 1.0000
Surface Tension (dyne/cm) 6.266 6.266
Thermal Conductivity (W/m-K) 7.568e-002 2.284e-002 7.568e-002
Viscosity (cP) 0.1069 9.069e-003 0.1069
Cv (Semi-Ideal) (kJ/kgmole-C) 201.3 149.6 201.3
Mass Cv (Semi-Ideal) (kJ/kg-C) 2.770 2.066 2.770
Mass Cv (kJ/kg-C) 2.770 1.943 2.770
Cv (Ent. Method) (kJ/kgmole-C)
Mass Cv (Ent. Method) (kJ/kg-C)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C (kPa) 126.1 129.1 126.1
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