Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 124

User Property                                                                                                            

Partial Pressure of H2S (kPa)   0.0000                                                                                    

Heat of Vap. (kJ/kgmole)        1.752e+004                                                                               

Kinematic Viscosity (cSt)       0.2534            0.4818            0.2534                                                

Liq. Mass Density (Std. Cond) (kg/m3) 562.9             562.9             562.9                                                

Liq. Vol. Flow (Std. Cond) (m3/h) 344.7             0.0000            344.7                                                 

Liquid Fraction                 1.000             0.0000            1.000                                                

Molar Volume (m3/kgmole)        0.1125            3.294             0.1125                                                

Mass Heat of Vap. (kJ/kg)       301.5                                                                                    

Phase Fraction [Molar Basis]    0.0000            0.0000            1.0000                                               

Surface Tension (dyne/cm)       7.207                               7.207                                                

Thermal Conductivity (W/m-K)    7.650e-002        1.875e-002        7.650e-002                                           

Viscosity (cP)                  0.1309            8.502e-003        0.1309                                               

Cv (Semi-Ideal) (kJ/kgmole-C)   147.3             103.4             147.3                                                

Mass Cv (Semi-Ideal) (kJ/kg-C)  2.534             1.779             2.534                                                

Mass Cv (kJ/kg-C)               2.534             1.664             2.534                                                

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)         497.3             497.4             497.3                                                

Liq. Vol. Flow - Sum(Std. Cond) (m3/h) 344.7             0.0000            344.7                                                

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              0.5144           0.0002           22.6826          0.0001           0.0448           0.0001          

i-Butane             3326.6088        0.9966           193355.8097      0.9966           344.0703         0.9967          

n-Butane             10.8875          0.0033           632.8232         0.0033           1.0850           0.0031          

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