Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 25

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          

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                                                                                                                  

------------------------------------------------------------------------------Куб_К1 (Материальный поток): Worksheet

------------------------------------------------------------------------------Материальный поток: Куб_К1                                                         Термодинамический пакет: Базис-1     

Пакет свойств: Peng-Robinson         

УСЛОВИЯ                                                                                                                 

Суммарная         Жидкая фаза                                                            

Доля пара/фазы                  0.0000            1.0000