Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 39

Mass Entropy (kJ/kg-C)          1.495             1.495                                                                  

Heat Capacity (kJ/kgmole-C)     160.9             160.9                                                                  

Mass Heat Capacity (kJ/kg-C)    2.769             2.769                                                                  

Lower Heating Value (kJ/kgmole) 2.657e+006        2.657e+006                                                             

Mass Lower Heating Value (kJ/kg) 4.571e+004        4.571e+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)   9.875             9.875                                                                   

Specific Heat (kJ/kgmole-C)     160.9             160.9                                                                  

Std. Gas Flow (STD_m3/h)        2.226e+004        2.226e+004                                                              

Std. Ideal Liq. Mass Density (kg/m3) 574.0             574.0                                                                  

Act. Liq. Flow (m3/s)           2.948e-002        2.948e-002                                                              

Z Factor                        3.079e-002        3.079e-002                                                             

Watson K                        13.63             13.63                                                                   

User Property                                                                                                            

Partial Pressure of H2S (kPa)   0.0000                                                                                    

Heat of Vap. (kJ/kgmole)        1.795e+004                                                                               

Kinematic Viscosity (cSt)       0.2312            0.2312                                                                  

Liq. Mass Density (Std. Cond) (kg/m3) 575.3             575.3                                                                  

Liq. Vol. Flow (Std. Cond) (m3/h) 95.12             95.12                                                                   

Liquid Fraction                 1.000             1.000                                                                  

Molar Volume (m3/kgmole)        0.1127            0.1127                                                                  

Mass Heat of Vap. (kJ/kg)       308.8                                                                                    

Phase Fraction [Molar Basis]    0.0000            1.0000                                                                 

Surface Tension (dyne/cm)       7.123             7.123                                                                  

Thermal Conductivity (W/m-K)    7.706e-002        7.706e-002                                                             

Viscosity (cP)                  0.1192            0.1192                                                                 

Cv (Semi-Ideal) (kJ/kgmole-C)   152.6             152.6                                                                  

Mass Cv (Semi-Ideal) (kJ/kg-C)  2.626             2.626