Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 24

User Property                                                                                                            

Partial Pressure of H2S (kPa)   0.0000                                                                                    

Heat of Vap. (kJ/kgmole)        3.954e+004                                                                               

Kinematic Viscosity (cSt)       0.4800            0.4800                                                                  

Liq. Mass Density (Std. Cond) (kg/m3) 1015              1015                                                                   

Liq. Vol. Flow (Std. Cond) (m3/h) 24.78             24.78                                                                   

Liquid Fraction                 1.000             1.000                                                                  

Molar Volume (m3/kgmole)        1.836e-002        1.836e-002                                                             

Mass Heat of Vap. (kJ/kg)       2195                                                                                     

Phase Fraction [Molar Basis]    0.0000            1.0000                                                                 

Surface Tension (dyne/cm)       66.16             66.16                                                                  

Thermal Conductivity (W/m-K)    0.6524            0.6524                                                                 

Viscosity (cP)                  0.4711            0.4711                                                                 

Cv (Semi-Ideal) (kJ/kgmole-C)   69.66             69.66                                                                  

Mass Cv (Semi-Ideal) (kJ/kg-C)  3.867             3.867                                                                  

Mass Cv (kJ/kg-C)               3.719             3.719                                                                  

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

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

Cp/Cv (Ent. Method)                                                                                                       

Reid VP at 37.8 C (kPa)                                                                                                  

True VP at 37.8 C (kPa)         6.467             6.467                                                                   

Liq. Vol. Flow - Sum(Std. Cond) (m3/h) 24.78             24.78                                                                  

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              0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

i-Butane             0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

n-Butane             0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

i-Pentane            0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

n-Pentane            0.0000           0.0000           0.0000           0.0000           0.0000           0.0000          

n-Hexane             0.0000           0.0000           0.0000           0.0000           0.0000           0.0000