Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 82

n-Butane             0.0415           0.0000           2.4139           0.0000           0.0041           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              20.2551          0.0087           324.9512         0.0032           1.0854           0.0054          

Итого                2329.2666        1.0000           101940.1457      1.0000           202.2396         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               31.4487          0.0135           945.6583         0.0093           2.6587           0.0131          

Propane              2260.7490        0.9706           99692.2497       0.9779           196.7566         0.9729          

i-Butane             16.7723          0.0072           974.8725         0.0096           1.7348           0.0086          

n-Butane             0.0415           0.0000           2.4139           0.0000           0.0041           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              20.2551          0.0087           324.9512         0.0032           1.0854           0.0054          

Итого                2329.2666        1.0000           101940.1457      1.0000           202.2396         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                                                                                                                  

------------------------------------------------------------------------------Boilup @COL1 (Материальный поток): Worksheet