Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 141

Molar Volume (m3/kgmole)        0.1127            0.1127                                                                  

Mass Heat of Vap. (kJ/kg)       308.8                                                                                    

Phase Fraction [Molar Basis]    0.0000            1.0000                                                                 

Surface Tension (dyne/cm)       7.123             7.123                                                                  

Thermal Conductivity (W/m-K)    7.706e-002        7.706e-002                                                             

Viscosity (cP)                  0.1192            0.1192                                                                 

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

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

Mass Cv (kJ/kg-C)               2.626             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             414.2                                                                  

True VP at 37.8 C (kPa)         415.2             415.2                                                                  

Liq. Vol. Flow - Sum(Std. Cond) (m3/h) 95.12             95.12                                                                  

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              0.0605           0.0001           2.6685           0.0000           0.0053           0.0001          

i-Butane             401.6317         0.4266           23344.4391       0.4266           41.5407          0.4357          

n-Butane             539.6547         0.5732           31366.8913       0.5732           53.7820          0.5641          

i-Pentane            0.1527           0.0002           11.0207          0.0002           0.0177           0.0002          

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                941.4997         1.0000           54725.0205       1.0000           95.3456          1.0000          

Жидкая 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