Heat Capacity (kJ/kgmole-C) 119.6 119.6
Mass Heat Capacity (kJ/kg-C) 2.796 2.796
Lower Heating Value (kJ/kgmole) 1.986e+006 1.986e+006
Mass Lower Heating Value (kJ/kg) 4.644e+004 4.644e+004
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) 11.65 11.65
Specific Heat (kJ/kgmole-C) 119.6 119.6
Std. Gas Flow (STD_m3/h) 5423 5423
Std. Ideal Liq. Mass Density (kg/m3) 498.4 498.4
Act. Liq. Flow (m3/s) 5.546e-003 5.546e-003
Z Factor 7.047e-002 7.047e-002
Watson K 14.84 14.84
User Property
Partial Pressure of H2S (kPa) 0.0000
Heat of Vap. (kJ/kgmole) 1.365e+004
Kinematic Viscosity (cSt) 0.2030 0.2030
Liq. Mass Density (Std. Cond) (kg/m3) 496.7 496.7
Liq. Vol. Flow (Std. Cond) (m3/h) 19.75 19.75
Liquid Fraction 1.000 1.000
Molar Volume (m3/kgmole) 8.706e-002 8.706e-002
Mass Heat of Vap. (kJ/kg) 319.2
Phase Fraction [Molar Basis] 0.0000 1.0000
Surface Tension (dyne/cm) 7.178 7.178
Thermal Conductivity (W/m-K) 9.653e-002 9.653e-002
Viscosity (cP) 9.972e-002 9.972e-002
Cv (Semi-Ideal) (kJ/kgmole-C) 111.3 111.3
Mass Cv (Semi-Ideal) (kJ/kg-C) 2.601 2.601
Mass Cv (kJ/kg-C) 1.737 1.737
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