Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 167

Std. Ideal Liq. Mass Density (kg/m3) 623.5             623.5             623.5                                                

Act. Liq. Flow (m3/s)           1.413e-003                          1.413e-003                                           

Z Factor                                          0.9112            1.330e-002                                           

Watson K                        13.05             13.05             13.05                                                 

User Property                                                                                                            

Partial Pressure of H2S (kPa)   0.0000                                                                                    

Heat of Vap. (kJ/kgmole)        2.268e+004                                                                               

Kinematic Viscosity (cSt)       0.2607            0.9185            0.2607                                                

Liq. Mass Density (Std. Cond) (kg/m3) 626.7             626.7             626.7                                                

Liq. Vol. Flow (Std. Cond) (m3/h) 4.659             0.0000            4.659                                                 

Liquid Fraction                 1.000             0.0000            1.000                                                

Molar Volume (m3/kgmole)        0.1257            8.616             0.1257                                                

Mass Heat of Vap. (kJ/kg)       314.3                                                                                    

Phase Fraction [Molar Basis]    0.0000            0.0000            1.0000                                               

Surface Tension (dyne/cm)       10.15                               10.15                                                

Thermal Conductivity (W/m-K)    8.930e-002        1.787e-002        8.930e-002                                           

Viscosity (cP)                  0.1496            7.692e-003        0.1496                                               

Cv (Semi-Ideal) (kJ/kgmole-C)   170.8             127.6             170.8                                                

Mass Cv (Semi-Ideal) (kJ/kg-C)  2.367             1.769             2.367                                                

Mass Cv (kJ/kg-C)               2.367             1.726             2.367                                                

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)         140.3             140.6             140.3                                                

Liq. Vol. Flow - Sum(Std. Cond) (m3/h) 4.659             0.0000            4.659                                                

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