Phase Fraction [Vol. Basis] 1.000
Phase Fraction [Mass Basis] 2.122e-314 1.000
Partial Pressure of CO2 (kPa) 0.0000
Cost Based on Flow (Cost/s) 0.0000 0.0000
Act. Gas Flow (ACT_m3/h)
Avg. Liq. Density (kgmole/m3) 10.07 10.07
Specific Heat (kJ/kgmole-C) 151.9 151.9
Std. Gas Flow (STD_m3/h) 2.931e+004 2.931e+004
Std. Ideal Liq. Mass Density (kg/m3) 565.4 565.4
Act. Liq. Flow (m3/s) 3.723e-002 3.723e-002
Z Factor 8.044e-002 8.044e-002
Watson K 13.75 13.75
User Property
Partial Pressure of H2S (kPa) 0.0000
Heat of Vap. (kJ/kgmole) 1.436e+004
Kinematic Viscosity (cSt) 0.2282 0.2282
Liq. Mass Density (Std. Cond) (kg/m3) 568.4 568.4
Liq. Vol. Flow (Std. Cond) (m3/h) 122.4 122.4
Liquid Fraction 1.000 1.000
Molar Volume (m3/kgmole) 0.1081 0.1081
Mass Heat of Vap. (kJ/kg) 255.9
Phase Fraction [Molar Basis] 0.0000 1.0000
Surface Tension (dyne/cm) 7.194 7.194
Thermal Conductivity (W/m-K) 7.979e-002 7.979e-002
Viscosity (cP) 0.1185 0.1185
Cv (Semi-Ideal) (kJ/kgmole-C) 143.6 143.6
Mass Cv (Semi-Ideal) (kJ/kg-C) 2.558 2.558
Mass Cv (kJ/kg-C) 1.867 1.867
Cv (Ent. Method) (kJ/kgmole-C)
Mass Cv (Ent. Method) (kJ/kg-C)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C (kPa) 567.1 567.1
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