Operational condition: Pressure, kPa = 101.33 (Gas)
| Temperature, K - Gas | Mole fraction of 2-Propen-1-ol (1) - Gas |
|---|---|
| 368.20 | 0.9030 |
| 366.33 | 0.8150 |
| 365.08 | 0.7540 |
| 363.52 | 0.6850 |
| 360.76 | 0.5680 |
| 359.42 | 0.5120 |
| 356.69 | 0.4350 |
| 352.37 | 0.3050 |
| 348.47 | 0.2110 |
| 347.68 | 0.1860 |
| 345.86 | 0.1440 |
| 343.81 | 0.0950 |
| 341.97 | 0.0600 |
| 339.19 | 0.0190 |
| 338.82 | 0.0120 |
Operational condition: Pressure, kPa = 101.33 (Gas)
| Temperature, K - Gas | Mole fraction of 2-Propen-1-ol (1) - Gas |
|---|---|
| 368.20 | 0.9030 |
| 366.33 | 0.8150 |
| 365.08 | 0.7540 |
| 363.52 | 0.6850 |
| 360.76 | 0.5680 |
| 359.42 | 0.5120 |
| 356.69 | 0.4350 |
| 352.37 | 0.3050 |
| 348.47 | 0.2110 |
| 347.68 | 0.1860 |
| 345.86 | 0.1440 |
| 343.81 | 0.0950 |
| 341.97 | 0.0600 |
| 339.19 | 0.0190 |
| 338.82 | 0.0120 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of 2-Propen-1-ol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.9670 | 368.20 |
| 0.9370 | 366.33 |
| 0.9070 | 365.08 |
| 0.8740 | 363.52 |
| 0.8110 | 360.76 |
| 0.7750 | 359.42 |
| 0.7070 | 356.69 |
| 0.5750 | 352.37 |
| 0.4550 | 348.47 |
| 0.4190 | 347.68 |
| 0.3550 | 345.86 |
| 0.2800 | 343.81 |
| 0.1970 | 341.97 |
| 0.0780 | 339.19 |
| 0.0570 | 338.82 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of 2-Propen-1-ol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.9670 | 368.20 |
| 0.9370 | 366.33 |
| 0.9070 | 365.08 |
| 0.8740 | 363.52 |
| 0.8110 | 360.76 |
| 0.7750 | 359.42 |
| 0.7070 | 356.69 |
| 0.5750 | 352.37 |
| 0.4550 | 348.47 |
| 0.4190 | 347.68 |
| 0.3550 | 345.86 |
| 0.2800 | 343.81 |
| 0.1970 | 341.97 |
| 0.0780 | 339.19 |
| 0.0570 | 338.82 |