Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 139

n-Pentane            0.0000           0.0000           0.0008           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                548.7925         1.0000           31900.1604       1.0000           54.7338          1.0000          

ЗНАЧЕНИЯ K                                                                                                              

Компоненты                             Объединенная жидкость      Легкая жидкость            Тяжелая жидкость           

Ethane                                                                                                                   

Propane                                                                                                                 

i-Butane                               1.269                      1.269                                                 

n-Butane                               0.9950                     0.9950                                                

i-Pentane                              0.5034                     0.5034                                                

n-Pentane                              0.4162                     0.4162                                                

n-Hexane                                                                                                                 

H2O                                                                                                                     

Methane                                                                                                                  

------------------------------------------------------------------------------Верх_К2 @COL3 (Материальный поток): Worksheet

------------------------------------------------------------------------------Материальный поток: Верх_К2 @COL3                                                  Термодинамический пакет: Базис-1     

Пакет свойств: Peng-Robinson         

УСЛОВИЯ                                                                                                                 

Суммарная         Жидкая фаза                                                            

Доля пара/фазы                  0.0000            1.0000                                                                 

Температура (C)                 61.48             61.48                                                                  

Давление (kPa)                  759.9             759.9                                                                  

Мольный расход (kgmole/h)       941.5             941.5                                                                  

Массовый расход (kg/h)          5.473e+004        5.473e+004                                                             

Станд.расход ид.жидкости (m3/h) 95.35             95.35                                                                  

Мольная энтальпия (kJ/kgmole)   -1.452e+005       -1.452e+005                                                            

Мольная энтропия (kJ/kgmole-C)  86.90             86.90                                                                  

Теплосодержание (kJ/h)          -1.367e+008       -1.367e+008                                                             

Расход жидкости @станд.усл. (m3/h) 95.12*            95.12                                                                  

СВОЙСТВА ПОТОКА                                                                                                          

Суммарная         Жидкая фаза