Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 87

Phase Fraction [Vol. Basis]                                         1.000                                                

Phase Fraction [Mass Basis]     2.122e-314        0.0000            1.000                                                

Partial Pressure of CO2 (kPa)   0.0000                                                                                   

Cost Based on Flow (Cost/s)     0.0000            0.0000            0.0000                                               

Act. Gas Flow (ACT_m3/h)                                                                                                 

Avg. Liq. Density (kgmole/m3)   9.798             9.814             9.798                                                

Specific Heat (kJ/kgmole-C)     221.2             156.7             221.2                                                

Std. Gas Flow (STD_m3/h)        9.446e+004        0.0000            9.446e+004                                           

Std. Ideal Liq. Mass Density (kg/m3) 576.3             574.3             576.3                                                

Act. Liq. Flow (m3/s)           0.1505                              0.1505                                               

Z Factor                                          0.6505            8.696e-002                                           

Watson K                        13.60             13.63             13.60                                                 

User Property                                                                                                            

Partial Pressure of H2S (kPa)   0.0000                                                                                    

Heat of Vap. (kJ/kgmole)        1.289e+004                                                                               

Kinematic Viscosity (cSt)       0.1785            0.1952            0.1785                                                

Liq. Mass Density (Std. Cond) (kg/m3) 578.0             575.9             578.0                                                

Liq. Vol. Flow (Std. Cond) (m3/h) 406.6             0.0000            406.6                                                 

Liquid Fraction                 1.000             0.0000            1.000                                                

Molar Volume (m3/kgmole)        0.1356            1.015             0.1356                                                

Mass Heat of Vap. (kJ/kg)       219.2                                                                                    

Phase Fraction [Molar Basis]    0.0000            0.0000            1.0000                                                

Surface Tension (dyne/cm)       2.541                               2.541                                                

Thermal Conductivity (W/m-K)    5.371e-002        2.714e-002        5.371e-002                                           

Viscosity (cP)                  7.741e-002        1.126e-002        7.741e-002                                           

Cv (Semi-Ideal) (kJ/kgmole-C)   212.9             148.4             212.9                                                

Mass Cv (Semi-Ideal) (kJ/kg-C)  3.620             2.535             3.620                                                

Mass Cv (kJ/kg-C)               3.620             1.961             3.620                                                

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

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

Cp/Cv (Ent. Method)                                                                                                       

Reid VP at 37.8 C (kPa)         402.5             414.0             402.5