Heat Capacity (kJ/kgmole-C) 111.7 111.7
Mass Heat Capacity (kJ/kg-C) 1.922 1.922
Lower Heating Value (kJ/kgmole) 2.653e+006 2.653e+006
Mass Lower Heating Value (kJ/kg) 4.564e+004 4.564e+004
Phase Fraction [Vol. Basis] 1.000
Phase Fraction [Mass Basis] 4.941e-324 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) 1.229e+004 1.229e+004
Avg. Liq. Density (kgmole/m3) 9.670 9.670
Specific Heat (kJ/kgmole-C) 111.7 111.7
Std. Gas Flow (STD_m3/h) 8.821e+004 8.821e+004
Std. Ideal Liq. Mass Density (kg/m3) 562.0 562.0
Act. Liq. Flow (m3/s)
Z Factor 0.8434 0.8434
Watson K 13.81 13.81
User Property
Partial Pressure of H2S (kPa) 0.0000
Heat of Vap. (kJ/kgmole) 1.752e+004
Kinematic Viscosity (cSt) 0.4818 0.4818
Liq. Mass Density (Std. Cond) (kg/m3) 562.9 562.9
Liq. Vol. Flow (Std. Cond) (m3/h) 385.2 385.2
Liquid Fraction 0.0000 0.0000
Molar Volume (m3/kgmole) 3.294 3.294
Mass Heat of Vap. (kJ/kg) 301.5
Phase Fraction [Molar Basis] 1.0000 1.0000
Surface Tension (dyne/cm)
Thermal Conductivity (W/m-K) 1.875e-002 1.875e-002
Viscosity (cP) 8.502e-003 8.502e-003
Cv (Semi-Ideal) (kJ/kgmole-C) 103.4 103.4
Mass Cv (Semi-Ideal) (kJ/kg-C) 1.779 1.779
Mass Cv (kJ/kg-C) 1.664 1.664
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