Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 31

Propane              214.1491         0.9337           9443.3315        0.9626           18.6377          0.9469          

i-Butane             0.9215           0.0040           53.5609          0.0055           0.0953           0.0048          

n-Butane             0.0019           0.0000           0.1086           0.0000           0.0002           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              8.2903           0.0361           133.0000         0.0136           0.4442           0.0226          

Итого                229.3488         1.0000           9810.0010        1.0000           19.6835          1.0000          

Паровая 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               5.9861           0.0261           180.0000         0.0183           0.5061           0.0257          

Propane              214.1491         0.9337           9443.3315        0.9626           18.6377          0.9469          

i-Butane             0.9215           0.0040           53.5609          0.0055           0.0953           0.0048          

n-Butane             0.0019           0.0000           0.1086           0.0000           0.0002           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              8.2903           0.0361           133.0000         0.0136           0.4442           0.0226          

Итого                229.3488         1.0000           9810.0010        1.0000           19.6835          1.0000          

ЗНАЧЕНИЯ K                                                                                                              

Компоненты                             Объединенная жидкость      Легкая жидкость            Тяжелая жидкость           

Ethane                                                                                                                   

Propane                                                                                                                 

i-Butane                                                                                                                 

n-Butane                                                                                                                

i-Pentane                                                                                                                

n-Pentane                                                                                                               

n-Hexane                                                                                                                 

H2O                                                                                                                     

Methane