Operational conditions:
Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0932 | 0.4580 |
0.1336 | 0.5890 |
0.2044 | 0.8100 |
0.2782 | 0.9820 |
0.3394 | 1.107 |
0.4353 | 1.147 |
0.5068 | 1.154 |
0.6727 | 1.001 |
0.8726 | 0.4520 |
Operational conditions:
Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0932 | 0.4580 |
0.1336 | 0.5890 |
0.2044 | 0.8100 |
0.2782 | 0.9820 |
0.3394 | 1.107 |
0.4353 | 1.147 |
0.5068 | 1.154 |
0.6727 | 1.001 |
0.8726 | 0.4520 |
Operational condition: Pressure, kPa = 94.7 (Liquid)
Mole fraction of Cyclohexane (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 416.95 |
0.1399 | 391.25 |
0.2808 | 377.35 |
0.4226 | 368.45 |
0.6373 | 360.25 |
0.7816 | 356.55 |
0.9269 | 353.45 |
1.0000 | 351.75 |
Operational condition: Pressure, kPa = 94.7 (Liquid)
Mole fraction of Cyclohexane (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 416.95 |
0.1399 | 391.25 |
0.2808 | 377.35 |
0.4226 | 368.45 |
0.6373 | 360.25 |
0.7816 | 356.55 |
0.9269 | 353.45 |
1.0000 | 351.75 |