Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 64

Phase Fraction [Vol. Basis]                       1.000                                                                  

Phase Fraction [Mass Basis]     2.122e-314        1.000                                                                  

Partial Pressure of CO2 (kPa)   0.0000                                                                                   

Cost Based on Flow (Cost/s)     0.0000            0.0000                                                                 

Act. Gas Flow (ACT_m3/h)                                                                                                 

Avg. Liq. Density (kgmole/m3)   8.509             8.509                                                                  

Specific Heat (kJ/kgmole-C)     165.0             165.0                                                                  

Std. Gas Flow (STD_m3/h)        670.6             670.6                                                                   

Std. Ideal Liq. Mass Density (kg/m3) 636.2             636.2                                                                  

Act. Liq. Flow (m3/s)           9.283e-004        9.283e-004                                                              

Z Factor                        1.510e-002        1.510e-002                                                             

Watson K                        12.99             12.99                                                                   

User Property                                                                                                            

Partial Pressure of H2S (kPa)   0.0000                                                                                    

Heat of Vap. (kJ/kgmole)        2.496e+004                                                                               

Kinematic Viscosity (cSt)       0.3894            0.3894                                                                  

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)        0.1178            0.1178                                                                  

Mass Heat of Vap. (kJ/kg)       333.8                                                                                    

Phase Fraction [Molar Basis]    0.0000            1.0000                                                                  

Surface Tension (dyne/cm)       16.44             16.44                                                                  

Thermal Conductivity (W/m-K)    0.1086            0.1086                                                                 

Viscosity (cP)                  0.2471            0.2471                                                                 

Cv (Semi-Ideal) (kJ/kgmole-C)   156.7             156.7                                                                  

Mass Cv (Semi-Ideal) (kJ/kg-C)  2.096             2.096                                                                  

Mass Cv (kJ/kg-C)               1.637             1.637                                                                  

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