Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 52

Partial Pressure of H2S (kPa)   0.0000                                                                                    

Heat of Vap. (kJ/kgmole)        2.479e+004                                                                               

Kinematic Viscosity (cSt)       0.2622            0.2622                                                                  

Liq. Mass Density (Std. Cond) (kg/m3) 638.1             638.1                                                                  

Liq. Vol. Flow (Std. Cond) (m3/h) 3.323             3.323                                                                   

Liquid Fraction                 1.000             1.000                                                                  

Molar Volume (m3/kgmole)        0.1315            0.1315                                                                  

Mass Heat of Vap. (kJ/kg)       331.5                                                                                    

Phase Fraction [Molar Basis]    0.0000            1.0000                                                                 

Surface Tension (dyne/cm)       9.994             9.994                                                                  

Thermal Conductivity (W/m-K)    9.006e-002        9.006e-002                                                             

Viscosity (cP)                  0.1491            0.1491                                                                 

Cv (Semi-Ideal) (kJ/kgmole-C)   186.6             186.6                                                                  

Mass Cv (Semi-Ideal) (kJ/kg-C)  2.495             2.495                                                                  

Mass Cv (kJ/kg-C)               2.495             2.495                                                                  

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

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

Cp/Cv (Ent. Method)                                                                                                       

Reid VP at 37.8 C (kPa)         94.65             94.65                                                                  

True VP at 37.8 C (kPa)         94.83             94.83                                                                   

Liq. Vol. Flow - Sum(Std. Cond) (m3/h) 3.323             3.323                                                                  

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            1.5450           0.0545           111.4704         0.0526           0.1788           0.0536          

n-Pentane            21.5354          0.7594           1553.7971        0.7328           2.4674           0.7403          

n-Hexane             5.2798           0.1862           455.0000         0.2146           0.6866           0.2060           

H2O                  0.0000           0.0000           0.0000           0.0000           0.0000           0.0000