Operational conditions:
Mole fraction of 1-Hexene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0500 | 0.0111 |
0.1000 | 0.0212 |
0.1499 | 0.0303 |
0.1998 | 0.0376 |
0.2496 | 0.0447 |
0.2998 | 0.0505 |
0.3500 | 0.0549 |
0.3984 | 0.0589 |
0.4492 | 0.0610 |
0.5005 | 0.0614 |
0.5498 | 0.0614 |
0.6000 | 0.0597 |
0.6496 | 0.0566 |
0.6992 | 0.0528 |
0.7497 | 0.0474 |
0.8000 | 0.0413 |
0.8499 | 0.0331 |
0.9000 | 0.0234 |
0.9500 | 0.0117 |
Operational conditions:
Mole fraction of 1-Hexene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0500 | 0.0111 |
0.1000 | 0.0212 |
0.1499 | 0.0303 |
0.1998 | 0.0376 |
0.2496 | 0.0447 |
0.2998 | 0.0505 |
0.3500 | 0.0549 |
0.3984 | 0.0589 |
0.4492 | 0.0610 |
0.5005 | 0.0614 |
0.5498 | 0.0614 |
0.6000 | 0.0597 |
0.6496 | 0.0566 |
0.6992 | 0.0528 |
0.7497 | 0.0474 |
0.8000 | 0.0413 |
0.8499 | 0.0331 |
0.9000 | 0.0234 |
0.9500 | 0.0117 |
Operational condition: Temperature, K = 313.15 (Liquid)
Mole fraction of Heptane (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
---|---|
0.3010 | 35.16 |
0.6977 | 22.32 |
Operational condition: Temperature, K = 313.15 (Liquid)
Mole fraction of Heptane (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
---|---|
0.3010 | 35.16 |
0.6977 | 22.32 |