Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 162

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              0.0000           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            1.5450           0.0545           111.4704         0.0526           0.1788           0.0536          

n-Pentane            21.5354          0.7594           1553.7971        0.7328           2.4674           0.7403          

n-Hexane             5.2798           0.1862           455.0000         0.2146           0.6866           0.2060          

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                28.3601          1.0000           2120.2675        1.0000           3.3328           1.0000          

ЗНАЧЕНИЯ K                                                                                                              

Компоненты                             Объединенная жидкость      Легкая жидкость            Тяжелая жидкость           

Ethane                                                                                                                   

Propane                                                                                                                 

i-Butane                                                                                                                 

n-Butane                                                                                                                

i-Pentane                              1.336                      1.336                                                 

n-Pentane                              1.106                      1.106                                                 

n-Hexane                               0.4701                     0.4701                                                

H2O                                                                                                                     

Methane                                                                                                                  

------------------------------------------------------------------------------Куб_К2 @COL4 (Материальный поток): Worksheet

------------------------------------------------------------------------------Материальный поток: Куб_К2 @COL4                                                   Термодинамический пакет: Базис-1     

Пакет свойств: Peng-Robinson         

УСЛОВИЯ                                                                                                                 

Суммарная         Жидкая фаза                                                            

Доля пара/фазы                  0.0000            1.0000                                                                 

Температура (C)                 110.1             110.1                                                                  

Давление (kPa)                  790.3             790.3