Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 160

Mass Entropy (kJ/kg-C)          1.457             2.371             1.457                                                

Heat Capacity (kJ/kgmole-C)     194.9             145.3             194.9                                                

Mass Heat Capacity (kJ/kg-C)    2.607             1.980             2.607                                                

Lower Heating Value (kJ/kgmole) 3.388e+006        3.327e+006        3.388e+006                                           

Mass Lower Heating Value (kJ/kg) 4.531e+004        4.534e+004        4.531e+004                                           

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)   8.509             8.620             8.509                                                

Specific Heat (kJ/kgmole-C)     194.9             145.3             194.9                                                

Std. Gas Flow (STD_m3/h)        670.6             0.0000            670.6                                                

Std. Ideal Liq. Mass Density (kg/m3) 636.2             632.5             636.2                                                

Act. Liq. Flow (m3/s)           1.036e-003                          1.036e-003                                           

Z Factor                                          0.9054            1.482e-002                                           

Watson K                        12.99             13.01             12.99                                                 

User Property                                                                                                            

Partial Pressure of H2S (kPa)   0.0000                                                                                    

Heat of Vap. (kJ/kgmole)        2.479e+004                                                                               

Kinematic Viscosity (cSt)       0.2622            0.8614            0.2622                                                

Liq. Mass Density (Std. Cond) (kg/m3) 638.1             634.1             638.1                                                

Liq. Vol. Flow (Std. Cond) (m3/h) 3.323             0.0000            3.323                                                 

Liquid Fraction                 1.000             0.0000            1.000                                                

Molar Volume (m3/kgmole)        0.1315            8.034             0.1315                                                

Mass Heat of Vap. (kJ/kg)       331.5                                                                                    

Phase Fraction [Molar Basis]    0.0000            0.0000            1.0000                                               

Surface Tension (dyne/cm)       9.994                               9.994                                                

Thermal Conductivity (W/m-K)    9.006e-002        1.912e-002        9.006e-002                                           

Viscosity (cP)                  0.1491            7.867e-003        0.1491                                               

Cv (Semi-Ideal) (kJ/kgmole-C)   186.6             136.9             186.6                                                

Mass Cv (Semi-Ideal) (kJ/kg-C)  2.495             1.866             2.495