Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 13

H2O                  0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

Methane              8.2903           0.0067           133.0000         0.0019           0.4442           0.0036           

Итого                1239.6752        1.0000           69575.0000       1.0000           123.0447         1.0000          

ЗНАЧЕНИЯ K                                                                                                              

Компоненты                             Объединенная жидкость      Легкая жидкость            Тяжелая жидкость           

Ethane                                 0.0000                     0.0000                                                

Propane                                0.0000                     0.0000                                                

i-Butane                               0.0000                     0.0000                                                

n-Butane                               0.0000                     0.0000                                                

i-Pentane                              0.0000                     0.0000                                                

n-Pentane                              0.0000                     0.0000                                                

n-Hexane                               0.0000                     0.0000                                                

H2O                                                                                                                     

Methane                                0.0000                     0.0000                                                

------------------------------------------------------------------------------1 (Материальный поток): Worksheet

------------------------------------------------------------------------------Материальный поток: 1                                                              Термодинамический пакет: Базис-1     

Пакет свойств: Peng-Robinson         

УСЛОВИЯ                                                                                                                 

Суммарная         Жидкая фаза                                                            

Доля пара/фазы                  0.0000            1.0000                                                                 

Температура (C)                 49.00*            49.00                                                                  

Давление (kPa)                  2080              2080                                                                   

Мольный расход (kgmole/h)       1240              1240                                                                   

Массовый расход (kg/h)          6.958e+004        6.958e+004                                                              

Станд.расход ид.жидкости (m3/h) 123.0             123.0                                                                  

Мольная энтальпия (kJ/kgmole)   -1.428e+005       -1.428e+005                                                             

Мольная энтропия (kJ/kgmole-C)  90.00             90.00                                                                  

Теплосодержание (kJ/h)          -1.770e+008       -1.770e+008                                                             

Расход жидкости @станд.усл. (m3/h) 122.4*            122.4                                                                  

СВОЙСТВА ПОТОКА                                                                                                          

Суммарная         Жидкая фаза                                                             

Cp/(Cp - R)                     1.059             1.059                                                                  

Cp/Cv                           1.447             1.447