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) 8.642 8.641 8.642
Specific Heat (kJ/kgmole-C) 179.1 135.9 179.1
Std. Gas Flow (STD_m3/h) 8180 0.0000 8180
Std. Ideal Liq. Mass Density (kg/m3) 623.5 623.5 623.5
Act. Liq. Flow (m3/s) 1.208e-002 1.208e-002
Z Factor 0.9112 1.330e-002
Watson K 13.05 13.05 13.05
User Property
Partial Pressure of H2S (kPa) 0.0000
Heat of Vap. (kJ/kgmole) 2.268e+004
Kinematic Viscosity (cSt) 0.2607 0.9185 0.2607
Liq. Mass Density (Std. Cond) (kg/m3) 626.7 626.7 626.7
Liq. Vol. Flow (Std. Cond) (m3/h) 39.83 0.0000 39.83
Liquid Fraction 1.000 0.0000 1.000
Molar Volume (m3/kgmole) 0.1257 8.616 0.1257
Mass Heat of Vap. (kJ/kg) 314.3
Phase Fraction [Molar Basis] 0.0000 0.0000 1.0000
Surface Tension (dyne/cm) 10.15 10.15
Thermal Conductivity (W/m-K) 8.930e-002 1.787e-002 8.930e-002
Viscosity (cP) 0.1496 7.692e-003 0.1496
Cv (Semi-Ideal) (kJ/kgmole-C) 170.8 127.6 170.8
Mass Cv (Semi-Ideal) (kJ/kg-C) 2.367 1.769 2.367
Mass Cv (kJ/kg-C) 2.367 1.726 2.367
Cv (Ent. Method) (kJ/kgmole-C)
Mass Cv (Ent. Method) (kJ/kg-C)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C (kPa)
True VP at 37.8 C (kPa) 140.3 140.6 140.3
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