Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 94

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)   10.07             10.07                                                                   

Specific Heat (kJ/kgmole-C)     151.9             151.9                                                                  

Std. Gas Flow (STD_m3/h)        2.931e+004        2.931e+004                                                              

Std. Ideal Liq. Mass Density (kg/m3) 565.4             565.4                                                                  

Act. Liq. Flow (m3/s)           3.723e-002        3.723e-002                                                              

Z Factor                        8.044e-002        8.044e-002                                                             

Watson K                        13.75             13.75                                                                   

User Property                                                                                                            

Partial Pressure of H2S (kPa)   0.0000                                                                                    

Heat of Vap. (kJ/kgmole)        1.436e+004                                                                               

Kinematic Viscosity (cSt)       0.2282            0.2282                                                                  

Liq. Mass Density (Std. Cond) (kg/m3) 568.4             568.4                                                                  

Liq. Vol. Flow (Std. Cond) (m3/h) 122.4             122.4                                                                   

Liquid Fraction                 1.000             1.000                                                                  

Molar Volume (m3/kgmole)        0.1081            0.1081                                                                  

Mass Heat of Vap. (kJ/kg)       255.9                                                                                    

Phase Fraction [Molar Basis]    0.0000            1.0000                                                                 

Surface Tension (dyne/cm)       7.194             7.194                                                                  

Thermal Conductivity (W/m-K)    7.979e-002        7.979e-002                                                             

Viscosity (cP)                  0.1185            0.1185                                                                 

Cv (Semi-Ideal) (kJ/kgmole-C)   143.6             143.6                                                                  

Mass Cv (Semi-Ideal) (kJ/kg-C)  2.558             2.558                                                                  

Mass Cv (kJ/kg-C)               1.867             1.867                                                                  

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

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

Cp/Cv (Ent. Method)                                                                                                       

Reid VP at 37.8 C (kPa)         567.1             567.1