Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 101

Viscosity (cP)                  0.1192            8.708e-003        0.1192                                               

Cv (Semi-Ideal) (kJ/kgmole-C)   152.6             107.3             152.6                                                

Mass Cv (Semi-Ideal) (kJ/kg-C)  2.626             1.846             2.626                                                

Mass Cv (kJ/kg-C)               2.626             1.720             2.626                                                

Cv (Ent. Method) (kJ/kgmole-C)                                                                                            

Mass Cv (Ent. Method) (kJ/kg-C)                                                                                          

Cp/Cv (Ent. Method)                                                                                                       

Reid VP at 37.8 C (kPa)         414.2             423.1             414.2                                                

True VP at 37.8 C (kPa)         415.2             423.8             415.2                                                

Liq. Vol. Flow - Sum(Std. Cond) (m3/h) 171.2             0.0000            171.2                                                

СОСТАВ ПОТОКА                                                                                                            

Общий поток                                                                                    Доля пара 0.0000         

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              0.1089           0.0001           4.8034           0.0000           0.0095           0.0001          

i-Butane             722.9370         0.4266           42019.9908       0.4266           74.7732          0.4357          

n-Butane             971.3785         0.5732           56460.4050       0.5732           96.8076          0.5641          

i-Pentane            0.2749           0.0002           19.8373          0.0002           0.0318           0.0002          

n-Pentane            0.0000           0.0000           0.0015           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                1694.6994        1.0000           98505.0380       1.0000           171.6221         1.0000          

Паровая фаза                                                                                   Доля фазы 0.0000         

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              0.0000           0.0001           0.0000           0.0001           0.0000           0.0001          

i-Butane             0.0000           0.4878           0.0000           0.4878           0.0000           0.4971          

n-Butane             0.0000           0.5120           0.0000           0.5120           0.0000           0.5027          

i-Pentane            0.0000           0.0001           0.0000           0.0001           0.0000           0.0001          

n-Pentane            0.0000           0.0000           0.0000           0.0000           0.0000           0.0000