Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 77

Mass Density (kg/m3)            438.5             44.90             438.5                                                 

Act. Volume Flow (m3/h)         210.1             0.0000            210.1                                                

Mass Enthalpy (kJ/kg)           -2640             -2400             -2640                                                

Mass Entropy (kJ/kg-C)          2.385             3.345             2.385                                                

Heat Capacity (kJ/kgmole-C)     155.1             100.8             155.1                                                

Mass Heat Capacity (kJ/kg-C)    3.534             2.358             3.534                                                

Lower Heating Value (kJ/kgmole) 2.035e+006        1.986e+006        2.035e+006                                           

Mass Lower Heating Value (kJ/kg) 4.638e+004        4.644e+004        4.638e+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)   11.50             11.65             11.50                                                

Specific Heat (kJ/kgmole-C)     155.1             100.8             155.1                                                

Std. Gas Flow (STD_m3/h)        4.965e+004        0.0000            4.965e+004                                           

Std. Ideal Liq. Mass Density (kg/m3) 504.7             498.4             504.7                                                

Act. Liq. Flow (m3/s)           5.837e-002                          5.837e-002                                           

Z Factor                                          0.7028            7.382e-002                                           

Watson K                        14.74             14.84             14.74                                                 

User Property                                                                                                            

Partial Pressure of H2S (kPa)   0.0000                                                                                    

Heat of Vap. (kJ/kgmole)        1.204e+004                                                                               

Kinematic Viscosity (cSt)       0.1690            0.2327            0.1690                                                

Liq. Mass Density (Std. Cond) (kg/m3) 505.8             496.7             505.8                                                

Liq. Vol. Flow (Std. Cond) (m3/h) 182.2             0.0000            182.2                                                 

Liquid Fraction                 1.000             0.0000            1.000                                                

Molar Volume (m3/kgmole)        0.1001            0.9526            0.1001                                                

Mass Heat of Vap. (kJ/kg)       274.5                                                                                    

Phase Fraction [Molar Basis]    0.0000            0.0000            1.0000                                               

Surface Tension (dyne/cm)       3.629                               3.629                                                

Thermal Conductivity (W/m-K)    7.766e-002        2.406e-002        7.766e-002