Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 117

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)   9.775             9.775                                                                   

Specific Heat (kJ/kgmole-C)     208.2             208.2                                                                  

Std. Gas Flow (STD_m3/h)        2.389e+004        2.389e+004                                                              

Std. Ideal Liq. Mass Density (kg/m3) 578.2             578.2                                                                  

Act. Liq. Flow (m3/s)           3.714e-002        3.714e-002                                                              

Z Factor                        8.489e-002        8.489e-002                                                             

Watson K                        13.58             13.58                                                                   

User Property                                                                                                            

Partial Pressure of H2S (kPa)   0.0000                                                                                    

Heat of Vap. (kJ/kgmole)        1.316e+004                                                                               

Kinematic Viscosity (cSt)       0.1823            0.1823                                                                  

Liq. Mass Density (Std. Cond) (kg/m3) 580.0             580.0                                                                  

Liq. Vol. Flow (Std. Cond) (m3/h) 103.0             103.0                                                                   

Liquid Fraction                 1.000             1.000                                                                  

Molar Volume (m3/kgmole)        0.1323            0.1323                                                                  

Mass Heat of Vap. (kJ/kg)       222.4                                                                                    

Phase Fraction [Molar Basis]    0.0000            1.0000                                                                 

Surface Tension (dyne/cm)       2.998             2.998                                                                  

Thermal Conductivity (W/m-K)    5.686e-002        5.686e-002                                                             

Viscosity (cP)                  8.148e-002        8.148e-002                                                             

Cv (Semi-Ideal) (kJ/kgmole-C)   199.9             199.9                                                                  

Mass Cv (Semi-Ideal) (kJ/kg-C)  3.379             3.379                                                                  

Mass Cv (kJ/kg-C)               2.350             2.350                                                                  

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

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

Cp/Cv (Ent. Method)                                                                                                       

Reid VP at 37.8 C (kPa)         392.0             392.0