Operational conditions:
Mole fraction of Hexane, tetradecafluoro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0000 | 0.0000 |
0.0500 | 0.7420 |
0.1000 | 1.259 |
0.1500 | 1.609 |
0.2000 | 1.839 |
0.2500 | 1.989 |
0.3000 | 2.085 |
0.3500 | 2.146 |
0.4000 | 2.186 |
0.4500 | 2.21 |
0.5000 | 2.218 |
0.5500 | 2.208 |
0.6000 | 2.173 |
0.6500 | 2.103 |
0.7000 | 1.991 |
0.7500 | 1.825 |
0.8000 | 1.598 |
0.8500 | 1.302 |
0.9000 | 0.9360 |
0.9500 | 0.5000 |
1.0000 | 0.0000 |
Operational conditions:
Mole fraction of Hexane, tetradecafluoro- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0000 | 0.0000 |
0.0500 | 0.7420 |
0.1000 | 1.259 |
0.1500 | 1.609 |
0.2000 | 1.839 |
0.2500 | 1.989 |
0.3000 | 2.085 |
0.3500 | 2.146 |
0.4000 | 2.186 |
0.4500 | 2.21 |
0.5000 | 2.218 |
0.5500 | 2.208 |
0.6000 | 2.173 |
0.6500 | 2.103 |
0.7000 | 1.991 |
0.7500 | 1.825 |
0.8000 | 1.598 |
0.8500 | 1.302 |
0.9000 | 0.9360 |
0.9500 | 0.5000 |
1.0000 | 0.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Mole fraction of Hexane, tetradecafluoro- (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.0500 | 311.80 |
0.0997 | 330.40 |
0.1986 | 340.20 |
0.2964 | 342.10 |
0.3976 | 341.10 |
0.4986 | 338.80 |
0.5956 | 331.70 |
0.6970 | 320.80 |
0.8011 | 297.60 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Mole fraction of Hexane, tetradecafluoro- (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.0500 | 311.80 |
0.0997 | 330.40 |
0.1986 | 340.20 |
0.2964 | 342.10 |
0.3976 | 341.10 |
0.4986 | 338.80 |
0.5956 | 331.70 |
0.6970 | 320.80 |
0.8011 | 297.60 |