Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 105

n-Butane             1511.0332        0.5732           87827.2963       0.5732           150.5896         0.5641          

i-Pentane            0.4277           0.0002           30.8581          0.0002           0.0495           0.0002          

n-Pentane            0.0000           0.0000           0.0023           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           0.0000           0.0000           0.0000           0.0000           0.0000          

Итого                2636.1991        1.0000           153230.0585      1.0000           266.9677         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               0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

Propane              0.1694           0.0001           7.4719           0.0000           0.0147           0.0001          

i-Butane             1124.5687        0.4266           65364.4299       0.4266           116.3139         0.4357          

n-Butane             1511.0332        0.5732           87827.2963       0.5732           150.5896         0.5641          

i-Pentane            0.4277           0.0002           30.8581          0.0002           0.0495           0.0002          

n-Pentane            0.0000           0.0000           0.0023           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           0.0000           0.0000           0.0000           0.0000           0.0000          

Итого                2636.1991        1.0000           153230.0585      1.0000           266.9677         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                                                                                                                  

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