Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 22

Водная фаза                                                                                    Доля фазы 1.000          

Компоненты           Мольный расход   Мольные доли     Массовый расход  Массовые доли    Объемный расход  Объемные доли   

(kgmole/h)                        (kg/h)                           жидкости (m3/h)  жидкости        

Ethane               0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

Propane              0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

i-Butane             0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

n-Butane             0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

i-Pentane            0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

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                  1395.7180        1.0000           25144.0000       1.0000           25.1947          1.0000          

Methane              0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

Итого                1395.7180        1.0000           25144.0000       1.0000           25.1947          1.0000          

ЗНАЧЕНИЯ K                                                                                                              

Компоненты                             Объединенная жидкость      Легкая жидкость            Тяжелая жидкость           

Ethane                                                                                                                   

Propane                                                                                                                 

i-Butane                                                                                                                 

n-Butane                                                                                                                

i-Pentane                                                                                                                

n-Pentane                                                                                                               

n-Hexane                                                                                                                 

H2O                                    0.0000                                                0.0000                     

Methane                                                                                                                  

------------------------------------------------------------------------------к_Т3 (Материальный поток): Worksheet

------------------------------------------------------------------------------Материальный поток: к_Т3                                                           Термодинамический пакет: Базис-1     

Пакет свойств: Peng-Robinson         

УСЛОВИЯ                                                                                                                 

Суммарная         Водная фаза                                                            

Доля пара/фазы                  0.0000            1.0000                                                                 

Температура (C)                 58.89             58.89                                                                  

Давление (kPa)                  270.0             270.0                                                                  

Мольный расход (kgmole/h)       1396              1396