Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 71

User Property                                                                                                            

Partial Pressure of H2S (kPa)   0.0000                                                                                    

Heat of Vap. (kJ/kgmole)        1.929e+004                                                                               

Kinematic Viscosity (cSt)       0.2828            0.1858            0.2828                                                

Liq. Mass Density (Std. Cond) (kg/m3) 419.5             496.7             419.5                                                

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

Liquid Fraction                 0.0000            1.000             0.0000                                               

Molar Volume (m3/kgmole)        0.9753            9.137e-002        0.9753                                               

Mass Heat of Vap. (kJ/kg)       536.1                                                                                    

Phase Fraction [Molar Basis]    1.0000            0.0000            1.0000                                               

Surface Tension (dyne/cm)                         5.677                                                                  

Thermal Conductivity (W/m-K)    2.450e-002        8.895e-002        2.450e-002                                           

Viscosity (cP)                  1.043e-002        8.699e-002        1.043e-002                                           

Cv (Semi-Ideal) (kJ/kgmole-C)   70.72             121.5             70.72                                                

Mass Cv (Semi-Ideal) (kJ/kg-C)  1.965             2.841             1.965                                                

Mass Cv (kJ/kg-C)               1.591             2.841             1.591                                                

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

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

Cp/Cv (Ent. Method)                                                                                                       

Reid VP at 37.8 C (kPa)         3444              1580              3444                                                 

True VP at 37.8 C (kPa)         5831              1982              5831                                                 

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

СОСТАВ ПОТОКА                                                                                                            

Общий поток                                                                                    Доля пара 1.0000         

Компоненты           Мольный расход   Мольные доли     Массовый расход  Массовые доли    Объемный расход  Объемные доли   

(kgmole/h)                        (kg/h)                           жидкости (m3/h)  жидкости        

Ethane               0.0000           0.0509           0.0000           0.0426           0.0000           0.0551          

Propane              0.0000           0.6833           0.0000           0.8373           0.0000           0.7616          

i-Butane             0.0000           0.0015           0.0000           0.0024           0.0000           0.0019          

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