Operational condition: Pressure, kPa = 101.325 (Liquid)
| Mole fraction of Propanal (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 370.27 |
| 0.0399 | 367.65 |
| 0.0800 | 364.40 |
| 0.1199 | 361.70 |
| 0.1599 | 359.08 |
| 0.1999 | 356.55 |
| 0.2399 | 354.10 |
| 0.2798 | 351.72 |
| 0.3198 | 349.43 |
| 0.3598 | 347.20 |
| 0.3998 | 345.11 |
| 0.4398 | 342.99 |
| 0.4799 | 340.99 |
| 0.5199 | 339.08 |
| 0.5602 | 337.23 |
| 0.6002 | 335.38 |
| 0.6402 | 333.77 |
| 0.6819 | 332.07 |
| 0.7201 | 330.58 |
| 0.7601 | 329.07 |
| 0.8001 | 327.63 |
| 0.8402 | 326.22 |
| 0.8801 | 324.89 |
| 0.9201 | 323.64 |
| 0.9601 | 322.35 |
| 1.0000 | 321.18 |
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Mole fraction of Propanal (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 370.27 |
| 0.0399 | 367.65 |
| 0.0800 | 364.40 |
| 0.1199 | 361.70 |
| 0.1599 | 359.08 |
| 0.1999 | 356.55 |
| 0.2399 | 354.10 |
| 0.2798 | 351.72 |
| 0.3198 | 349.43 |
| 0.3598 | 347.20 |
| 0.3998 | 345.11 |
| 0.4398 | 342.99 |
| 0.4799 | 340.99 |
| 0.5199 | 339.08 |
| 0.5602 | 337.23 |
| 0.6002 | 335.38 |
| 0.6402 | 333.77 |
| 0.6819 | 332.07 |
| 0.7201 | 330.58 |
| 0.7601 | 329.07 |
| 0.8001 | 327.63 |
| 0.8402 | 326.22 |
| 0.8801 | 324.89 |
| 0.9201 | 323.64 |
| 0.9601 | 322.35 |
| 1.0000 | 321.18 |