Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 44

n-Pentane            0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

n-Hexane             0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

H2O                  0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

Methane              0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

Итого                392.7071         1.0000           22824.8601       1.0000           40.6118          1.0000          

ЗНАЧЕНИЯ K                                                                                                              

Компоненты                             Объединенная жидкость      Легкая жидкость            Тяжелая жидкость           

Ethane                                                                                                                   

Propane                                0.0000                     0.0000                                                

i-Butane                               0.0000                     0.0000                                                

n-Butane                               0.0000                     0.0000                                                

i-Pentane                                                                                                                

n-Pentane                                                                                                               

n-Hexane                                                                                                                 

H2O                                                                                                                     

Methane                                                                                                                  

------------------------------------------------------------------------------Куб_К3 (Материальный поток): Worksheet

------------------------------------------------------------------------------Материальный поток: Куб_К3                                                         Термодинамический пакет: Базис-1     

Пакет свойств: Peng-Robinson         

УСЛОВИЯ                                                                                                                 

Суммарная         Жидкая фаза                                                            

Доля пара/фазы                  0.0000            1.0000                                                                 

Температура (C)                 67.66             67.66                                                                  

Давление (kPa)                  770.1             770.1                                                                  

Мольный расход (kgmole/h)       548.8             548.8                                                                  

Массовый расход (kg/h)          3.190e+004        3.190e+004                                                             

Станд.расход ид.жидкости (m3/h) 54.73             54.73                                                                  

Мольная энтальпия (kJ/kgmole)   -1.415e+005       -1.415e+005                                                             

Мольная энтропия (kJ/kgmole-C)  70.14             70.14                                                                  

Теплосодержание (kJ/h)          -7.766e+007       -7.766e+007                                                             

Расход жидкости @станд.усл. (m3/h) 54.61*            54.61                                                                  

СВОЙСТВА ПОТОКА                                                                                                          

Суммарная         Жидкая фаза