Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 132

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                3572.9885        1.0000           207683.4088      1.0000           356.4118         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                                                                                                                  

------------------------------------------------------------------------------To Reboiler @COL3 (Материальный поток): Worksheet

------------------------------------------------------------------------------Материальный поток: To Reboiler @COL3                                              Термодинамический пакет: Базис-1     

Пакет свойств: Peng-Robinson         

УСЛОВИЯ                                                                                                                 

Суммарная         Паровая фаза      Жидкая фаза                                          

Доля пара/фазы                  0.0000            0.0000            1.0000                                               

Температура (C)                 67.60             67.60             67.60                                                

Давление (kPa)                  770.1             770.1             770.1                                                

Мольный расход (kgmole/h)       4122              0.0000            4122                                                 

Массовый расход (kg/h)          2.396e+005        0.0000            2.396e+005                                           

Станд.расход ид.жидкости (m3/h) 411.1             0.0000            411.1                                                

Мольная энтальпия (kJ/kgmole)   -1.415e+005       -1.233e+005       -1.415e+005                                          

Мольная энтропия (kJ/kgmole-C)  70.39             124.3             70.39                                                

Теплосодержание (kJ/h)          -5.834e+008       0.0000            -5.834e+008                                          

Расход жидкости @станд.усл. (m3/h) 410.2*            0.0000            410.2                                                

СВОЙСТВА ПОТОКА                                                                                                          

Суммарная         Паровая фаза      Жидкая фаза                                           

Cp/(Cp - R)                     1.054             1.076             1.054