Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 102

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                0.0000           1.0000           0.0000           1.0000           0.0000           1.0000          

Жидкая 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              0.1089           0.0001           4.8034           0.0000           0.0095           0.0001          

i-Butane             722.9370         0.4266           42019.9908       0.4266           74.7732          0.4357          

n-Butane             971.3785         0.5732           56460.4050       0.5732           96.8076          0.5641          

i-Pentane            0.2749           0.0002           19.8373          0.0002           0.0318           0.0002          

n-Pentane            0.0000           0.0000           0.0015           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                1694.6994        1.0000           98505.0380       1.0000           171.6221         1.0000          

ЗНАЧЕНИЯ K                                                                                                              

Компоненты                             Объединенная жидкость      Легкая жидкость            Тяжелая жидкость           

Ethane                                                                                                                   

Propane                                2.296                      2.296                                                 

i-Butane                               1.144                      1.144                                                 

n-Butane                               0.8932                     0.8932                                                

i-Pentane                              0.4435                     0.4435                                                

n-Pentane                              0.3648                     0.3648                                                

n-Hexane                                                                                                                 

H2O                                                                                                                     

Methane                                                                                                                  

------------------------------------------------------------------------------To Condenser @COL2 (Материальный поток): Worksheet

------------------------------------------------------------------------------Материальный поток: To Condenser @COL2                                             Термодинамический пакет: Базис-1     

Пакет свойств: Peng-Robinson         

УСЛОВИЯ                                                                                                                 

Суммарная         Паровая фаза