Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 100

Mass Density (kg/m3)            515.7             19.01             515.7                                                 

Act. Volume Flow (m3/h)         191.0             0.0000            191.0                                                

Mass Enthalpy (kJ/kg)           -2498             -2199             -2498                                                

Mass Entropy (kJ/kg-C)          1.495             2.449             1.495                                                

Heat Capacity (kJ/kgmole-C)     160.9             115.6             160.9                                                

Mass Heat Capacity (kJ/kg-C)    2.769             1.989             2.769                                                

Lower Heating Value (kJ/kgmole) 2.657e+006        2.656e+006        2.657e+006                                           

Mass Lower Heating Value (kJ/kg) 4.571e+004        4.570e+004        4.571e+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)   9.875             9.852             9.875                                                

Specific Heat (kJ/kgmole-C)     160.9             115.6             160.9                                                

Std. Gas Flow (STD_m3/h)        4.007e+004        0.0000            4.007e+004                                           

Std. Ideal Liq. Mass Density (kg/m3) 574.0             572.7             574.0                                                

Act. Liq. Flow (m3/s)           5.306e-002                          5.306e-002                                           

Z Factor                                          0.8350            3.079e-002                                           

Watson K                        13.63             13.65             13.63                                                 

User Property                                                                                                            

Partial Pressure of H2S (kPa)   0.0000                                                                                    

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

Kinematic Viscosity (cSt)       0.2312            0.4580            0.2312                                                

Liq. Mass Density (Std. Cond) (kg/m3) 575.3             574.0             575.3                                                

Liq. Vol. Flow (Std. Cond) (m3/h) 171.2             0.0000            171.2                                                 

Liquid Fraction                 1.000             0.0000            1.000                                                

Molar Volume (m3/kgmole)        0.1127            3.057             0.1127                                                

Mass Heat of Vap. (kJ/kg)       308.8                                                                                    

Phase Fraction [Molar Basis]    0.0000            0.0000            1.0000                                               

Surface Tension (dyne/cm)       7.123                               7.123                                                

Thermal Conductivity (W/m-K)    7.706e-002        1.994e-002        7.706e-002