Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 23

Массовый расход (kg/h)          2.514e+004        2.514e+004                                                             

Станд.расход ид.жидкости (m3/h) 25.19             25.19                                                                  

Мольная энтальпия (kJ/kgmole)   -2.836e+005       -2.836e+005                                                             

Мольная энтропия (kJ/kgmole-C)  62.08             62.08                                                                  

Теплосодержание (kJ/h)          -3.958e+008       -3.958e+008                                                             

Расход жидкости @станд.усл. (m3/h) 24.78*            24.78                                                                  

СВОЙСТВА ПОТОКА                                                                                                          

Суммарная         Водная фаза                                                             

Cp/(Cp - R)                     1.119             1.119                                                                  

Cp/Cv                           1.164             1.164                                                                   

Cv (kJ/kgmole-C)                67.00             67.00                                                                  

Molecular Weight                18.02             18.02                                                                   

Molar Density (kgmole/m3)       54.47             54.47                                                                  

Mass Density (kg/m3)            981.4             981.4                                                                  

Act. Volume Flow (m3/h)         25.62             25.62                                                                  

Mass Enthalpy (kJ/kg)           -1.574e+004       -1.574e+004                                                            

Mass Entropy (kJ/kg-C)          3.446             3.446                                                                  

Heat Capacity (kJ/kgmole-C)     77.98             77.98                                                                  

Mass Heat Capacity (kJ/kg-C)    4.328             4.328                                                                  

Lower Heating Value (kJ/kgmole) 0.0000            0.0000                                                                 

Mass Lower Heating Value (kJ/kg)                                                                                           

Phase Fraction [Vol. Basis]                       1.000                                                                  

Phase Fraction [Mass Basis]     0.0000            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)   55.40             55.40                                                                   

Specific Heat (kJ/kgmole-C)     77.98             77.98                                                                  

Std. Gas Flow (STD_m3/h)        3.300e+004        3.300e+004                                                              

Std. Ideal Liq. Mass Density (kg/m3) 998.0             998.0                                                                  

Act. Liq. Flow (m3/s)           7.117e-003        7.117e-003                                                              

Z Factor                        1.795e-003        1.795e-003                                                             

Watson K