Оптимизация рекуперативного теплообмена технологических потоков центральной газофракционирующей установки методом пинч-анализа, страница 90

Теплосодержание (kJ/h)          -1.393e+008       0.0000            -1.393e+008                                          

Расход жидкости @станд.усл. (m3/h) 103.0*            0.0000            103.0                                                

СВОЙСТВА ПОТОКА                                                                                                          

Суммарная         Паровая фаза      Жидкая фаза                                           

Cp/(Cp - R)                     1.039             1.056             1.039                                                

Cp/Cv                           1.039             1.361             1.039                                                 

Cv (kJ/kgmole-C)                213.6             115.5             213.6                                                

Molecular Weight                59.15             58.71             59.15                                                 

Molar Density (kgmole/m3)       7.347             0.9810            7.347                                                

Mass Density (kg/m3)            434.6             57.59             434.6                                                 

Act. Volume Flow (m3/h)         137.5             0.0000            137.5                                                

Mass Enthalpy (kJ/kg)           -2331             -2126             -2331                                                

Mass Entropy (kJ/kg-C)          1.917             2.498             1.917                                                

Heat Capacity (kJ/kgmole-C)     221.9             157.2             221.9                                                

Mass Heat Capacity (kJ/kg-C)    3.751             2.678             3.751                                                

Lower Heating Value (kJ/kgmole) 2.702e+006        2.682e+006        2.702e+006                                           

Mass Lower Heating Value (kJ/kg) 4.567e+004        4.568e+004        4.567e+004                                           

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)   9.775             9.805             9.775                                                

Specific Heat (kJ/kgmole-C)     221.9             157.2             221.9                                                

Std. Gas Flow (STD_m3/h)        2.389e+004        0.0000            2.389e+004                                           

Std. Ideal Liq. Mass Density (kg/m3) 578.2             575.7             578.2                                                

Act. Liq. Flow (m3/s)           3.820e-002                          3.820e-002                                           

Z Factor                                          0.6515            8.698e-002                                           

Watson K                        13.58             13.61             13.58                                                 

User Property                                                                                                            

Partial Pressure of H2S (kPa)   0.0000                                                                                    

Heat of Vap. (kJ/kgmole)        1.307e+004                                                                               

Kinematic Viscosity (cSt)       0.1779            0.1957            0.1779