Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 21

Kinematic Viscosity (cSt)       0.2808            0.2808                                                                  

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)        1.909e-002        1.909e-002                                                              

Mass Heat of Vap. (kJ/kg)       2185                                                                                     

Phase Fraction [Molar Basis]    0.0000            1.0000                                                                 

Surface Tension (dyne/cm)       57.65             57.65                                                                  

Thermal Conductivity (W/m-K)    0.6826            0.6826                                                                 

Viscosity (cP)                  0.2650            0.2650                                                                 

Cv (Semi-Ideal) (kJ/kgmole-C)   71.13             71.13                                                                  

Mass Cv (Semi-Ideal) (kJ/kg-C)  3.948             3.948                                                                  

Mass Cv (kJ/kg-C)               3.747             3.747                                                                  

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*         

H2O                  1395.7180        1.0000           25144.0000       1.0000           25.1947          1.0000          

Methane              0.0000           0.0000           0.0000           0.0000           0.0000           0.0000           

Итого                1395.7180        1.0000           25144.0000       1.0000           25.1947          1.0000