Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 79

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           0.0361           0.0000           0.0136           0.0000           0.0226          

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               25.4626          0.0121           765.6583         0.0083           2.1526           0.0118          

Propane              2046.6000        0.9746           90248.9183       0.9796           178.1189         0.9757          

i-Butane             15.8508          0.0075           921.3116         0.0100           1.6394           0.0090          

n-Butane             0.0397           0.0000           2.3053           0.0000           0.0040           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              11.9649          0.0057           191.9512         0.0021           0.6411           0.0035          

Итого                2099.9179        1.0000           92130.1447       1.0000           182.5560         1.0000          

ЗНАЧЕНИЯ K                                                                                                              

Компоненты                             Объединенная жидкость      Легкая жидкость            Тяжелая жидкость           

Ethane                                 2.153                      2.153                                                 

Propane                                0.9581                     0.9581                                                

i-Butane                               0.5323                     0.5323                                                

n-Butane                               0.4315                     0.4315                                                

i-Pentane                                                                                                                

n-Pentane                                                                                                               

n-Hexane                                                                                                                 

H2O                                                                                                                     

Methane                                6.344                      6.344                                                 

------------------------------------------------------------------------------To Condenser @COL1 (Материальный поток): Worksheet

------------------------------------------------------------------------------Материальный поток: To Condenser @COL1                                             Термодинамический пакет: Базис-1     

Пакет свойств: Peng-Robinson         

УСЛОВИЯ                                                                                                                 

Суммарная         Паровая фаза