Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 48

Теплосодержание (kJ/h)          -7.003e+006       -7.003e+006                                                             

Расход жидкости @станд.усл. (m3/h) 4.659*            4.659                                                                  

СВОЙСТВА ПОТОКА                                                                                                          

Суммарная         Жидкая фаза                                                             

Cp/(Cp - R)                     1.049             1.049                                                                  

Cp/Cv                           1.049             1.049                                                                   

Cv (kJ/kgmole-C)                170.8             170.8                                                                  

Molecular Weight                72.15             72.15                                                                   

Molar Density (kgmole/m3)       7.953             7.953                                                                  

Mass Density (kg/m3)            573.8             573.8                                                                   

Act. Volume Flow (m3/h)         5.088             5.088                                                                  

Mass Enthalpy (kJ/kg)           -2398             -2398                                                                  

Mass Entropy (kJ/kg-C)          0.8064            0.8064                                                                 

Heat Capacity (kJ/kgmole-C)     179.1             179.1                                                                  

Mass Heat Capacity (kJ/kg-C)    2.482             2.482                                                                  

Lower Heating Value (kJ/kgmole) 3.266e+006        3.266e+006                                                             

Mass Lower Heating Value (kJ/kg) 4.526e+004        4.526e+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)   8.642             8.642                                                                  

Specific Heat (kJ/kgmole-C)     179.1             179.1                                                                  

Std. Gas Flow (STD_m3/h)        956.8             956.8                                                                   

Std. Ideal Liq. Mass Density (kg/m3) 623.5             623.5                                                                  

Act. Liq. Flow (m3/s)           1.413e-003        1.413e-003                                                              

Z Factor                        1.330e-002        1.330e-002                                                             

Watson K                        13.05             13.05                                                                   

User Property                                                                                                            

Partial Pressure of H2S (kPa)   0.0000                                                                                    

Heat of Vap. (kJ/kgmole)        2.268e+004                                                                               

Kinematic Viscosity (cSt)       0.2607            0.2607