Operational conditions:
Mole fraction of 1-Hexene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0501 | 0.0101 |
0.1001 | 0.0188 |
0.1501 | 0.0271 |
0.2075 | 0.0350 |
0.2499 | 0.0405 |
0.2998 | 0.0454 |
0.3500 | 0.0499 |
0.3998 | 0.0534 |
0.4498 | 0.0543 |
0.4998 | 0.0559 |
0.5497 | 0.0559 |
0.5997 | 0.0548 |
0.6499 | 0.0525 |
0.6997 | 0.0489 |
0.7500 | 0.0440 |
0.7994 | 0.0379 |
0.8498 | 0.0310 |
0.9000 | 0.0219 |
0.9500 | 0.0114 |
Operational conditions:
Mole fraction of 1-Hexene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0501 | 0.0101 |
0.1001 | 0.0188 |
0.1501 | 0.0271 |
0.2075 | 0.0350 |
0.2499 | 0.0405 |
0.2998 | 0.0454 |
0.3500 | 0.0499 |
0.3998 | 0.0534 |
0.4498 | 0.0543 |
0.4998 | 0.0559 |
0.5497 | 0.0559 |
0.5997 | 0.0548 |
0.6499 | 0.0525 |
0.6997 | 0.0489 |
0.7500 | 0.0440 |
0.7994 | 0.0379 |
0.8498 | 0.0310 |
0.9000 | 0.0219 |
0.9500 | 0.0114 |
Operational condition: Temperature, K = 313.15 (Liquid)
Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
---|---|
0.6962 | 22.92 |
0.3007 | 35.40 |
Operational condition: Temperature, K = 313.15 (Liquid)
Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
---|---|
0.6962 | 22.92 |
0.3007 | 35.40 |