Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 69

Паровая фаза                                                                                   Доля фазы 0.0000         

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

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

Ethane               0.0000           0.0509           0.0000           0.0426           0.0000           0.0551          

Propane              0.0000           0.6833           0.0000           0.8373           0.0000           0.7616          

i-Butane             0.0000           0.0015           0.0000           0.0024           0.0000           0.0019          

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                  0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

Methane              0.0000           0.2643           0.0000           0.1178           0.0000           0.1814          

Итого                0.0000           1.0000           0.0000           1.0000           0.0000           1.0000          

ЗНАЧЕНИЯ K                                                                                                              

Компоненты                             Объединенная жидкость      Легкая жидкость            Тяжелая жидкость           

Ethane                                 1.951                      1.951                                                 

Propane                                0.7318                     0.7318                                                

i-Butane                               0.3622                     0.3622                                                

n-Butane                               0.2787                     0.2787                                                

i-Pentane                                                                                                                

n-Pentane                                                                                                               

n-Hexane                                                                                                                 

H2O                                                                                                                     

Methane                                7.312                      7.312                                                 

------------------------------------------------------------------------------4 (Материальный поток): Worksheet

------------------------------------------------------------------------------Материальный поток: 4                                                              Термодинамический пакет: Базис-1     

Пакет свойств: Peng-Robinson         

УСЛОВИЯ                                                                                                                 

Суммарная         Жидкая фаза       Паровая фаза                                         

Доля пара/фазы                  1.0000            0.0000            1.0000                                               

Температура (C)                 32.40             32.40             32.40                                                

Давление (kPa)                  1986              1986              1986                                                 

Мольный расход (kgmole/h)       0.0000            0.0000            0.0000