Operational condition: Pressure, kPa = 100 (Liquid)
| Mole fraction of Cyclohexane (2) - Liquid | Mole fraction of Cyclohexane (2) - Gas |
|---|---|
| 0.0130 | 0.1170 |
| 0.0260 | 0.1990 |
| 0.0580 | 0.3680 |
| 0.0780 | 0.4500 |
| 0.1180 | 0.5610 |
| 0.1560 | 0.6250 |
| 0.1900 | 0.6650 |
| 0.2230 | 0.7100 |
| 0.2730 | 0.7460 |
| 0.2830 | 0.7560 |
| 0.3270 | 0.7830 |
| 0.3720 | 0.8030 |
| 0.4060 | 0.8100 |
| 0.4680 | 0.8280 |
| 0.5230 | 0.8470 |
| 0.6030 | 0.8620 |
| 0.6520 | 0.8670 |
| 0.6960 | 0.8810 |
| 0.7430 | 0.8890 |
| 0.7860 | 0.9010 |
| 0.8320 | 0.9130 |
| 0.8920 | 0.9390 |
| 0.9460 | 0.9640 |
| 0.9960 | 0.9960 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Mole fraction of Cyclohexane (2) - Liquid | Mole fraction of Cyclohexane (2) - Gas |
|---|---|
| 0.0130 | 0.1170 |
| 0.0260 | 0.1990 |
| 0.0580 | 0.3680 |
| 0.0780 | 0.4500 |
| 0.1180 | 0.5610 |
| 0.1560 | 0.6250 |
| 0.1900 | 0.6650 |
| 0.2230 | 0.7100 |
| 0.2730 | 0.7460 |
| 0.2830 | 0.7560 |
| 0.3270 | 0.7830 |
| 0.3720 | 0.8030 |
| 0.4060 | 0.8100 |
| 0.4680 | 0.8280 |
| 0.5230 | 0.8470 |
| 0.6030 | 0.8620 |
| 0.6520 | 0.8670 |
| 0.6960 | 0.8810 |
| 0.7430 | 0.8890 |
| 0.7860 | 0.9010 |
| 0.8320 | 0.9130 |
| 0.8920 | 0.9390 |
| 0.9460 | 0.9640 |
| 0.9960 | 0.9960 |
Operational conditions:
| Mole fraction of Cyclohexane (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1000 | 0.6120 |
| 0.2010 | 1.093 |
| 0.3000 | 1.482 |
| 0.4010 | 1.75 |
| 0.5000 | 1.865 |
| 0.6000 | 1.825 |
| 0.7000 | 1.641 |
| 0.8010 | 1.304 |
| 0.9000 | 0.8140 |
Operational conditions:
| Mole fraction of Cyclohexane (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1000 | 0.6120 |
| 0.2010 | 1.093 |
| 0.3000 | 1.482 |
| 0.4010 | 1.75 |
| 0.5000 | 1.865 |
| 0.6000 | 1.825 |
| 0.7000 | 1.641 |
| 0.8010 | 1.304 |
| 0.9000 | 0.8140 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Mole fraction of Cyclohexane (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0130 | 396.86 |
| 0.0260 | 393.57 |
| 0.0580 | 387.92 |
| 0.0780 | 383.78 |
| 0.1180 | 379.05 |
| 0.1560 | 374.05 |
| 0.1900 | 371.83 |
| 0.2230 | 368.97 |
| 0.2730 | 367.54 |
| 0.2830 | 365.82 |
| 0.3270 | 364.24 |
| 0.3720 | 362.55 |
| 0.4060 | 361.65 |
| 0.4680 | 360.13 |
| 0.5230 | 359.24 |
| 0.6030 | 357.84 |
| 0.6520 | 357.43 |
| 0.6960 | 356.81 |
| 0.7430 | 356.13 |
| 0.7860 | 355.67 |
| 0.8320 | 355.16 |
| 0.8920 | 354.50 |
| 0.9460 | 353.91 |
| 0.9960 | 353.41 |
Operational condition: Pressure, kPa = 100 (Liquid)
| Mole fraction of Cyclohexane (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0130 | 396.86 |
| 0.0260 | 393.57 |
| 0.0580 | 387.92 |
| 0.0780 | 383.78 |
| 0.1180 | 379.05 |
| 0.1560 | 374.05 |
| 0.1900 | 371.83 |
| 0.2230 | 368.97 |
| 0.2730 | 367.54 |
| 0.2830 | 365.82 |
| 0.3270 | 364.24 |
| 0.3720 | 362.55 |
| 0.4060 | 361.65 |
| 0.4680 | 360.13 |
| 0.5230 | 359.24 |
| 0.6030 | 357.84 |
| 0.6520 | 357.43 |
| 0.6960 | 356.81 |
| 0.7430 | 356.13 |
| 0.7860 | 355.67 |
| 0.8320 | 355.16 |
| 0.8920 | 354.50 |
| 0.9460 | 353.91 |
| 0.9960 | 353.41 |