Operational condition: Pressure, kPa = 101.4 (Gas)
| Mole fraction of n-Hexane (1) - Liquid | Mole fraction of n-Hexane (1) - Gas |
|---|---|
| 0.0390 | 0.0890 |
| 0.1520 | 0.2800 |
| 0.2390 | 0.4130 |
| 0.3330 | 0.5230 |
| 0.4630 | 0.6190 |
| 0.5810 | 0.6890 |
| 0.6670 | 0.7430 |
| 0.7310 | 0.7820 |
| 0.7750 | 0.8150 |
| 0.7950 | 0.8290 |
| 0.8020 | 0.8360 |
| 0.8080 | 0.8410 |
| 0.8290 | 0.8500 |
| 0.8640 | 0.8740 |
| 0.9540 | 0.9530 |
Operational condition: Pressure, kPa = 101.4 (Gas)
| Mole fraction of n-Hexane (1) - Liquid | Mole fraction of n-Hexane (1) - Gas |
|---|---|
| 0.0390 | 0.0890 |
| 0.1520 | 0.2800 |
| 0.2390 | 0.4130 |
| 0.3330 | 0.5230 |
| 0.4630 | 0.6190 |
| 0.5810 | 0.6890 |
| 0.6670 | 0.7430 |
| 0.7310 | 0.7820 |
| 0.7750 | 0.8150 |
| 0.7950 | 0.8290 |
| 0.8020 | 0.8360 |
| 0.8080 | 0.8410 |
| 0.8290 | 0.8500 |
| 0.8640 | 0.8740 |
| 0.9540 | 0.9530 |
Operational condition: Pressure, kPa = 101.4 (Gas)
| Mole fraction of n-Hexane (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0390 | 355.80 |
| 0.1520 | 351.70 |
| 0.2390 | 349.00 |
| 0.3330 | 347.00 |
| 0.4630 | 344.90 |
| 0.5810 | 343.70 |
| 0.6670 | 343.00 |
| 0.7310 | 342.60 |
| 0.7750 | 342.30 |
| 0.7950 | 342.10 |
| 0.8020 | 342.10 |
| 0.8080 | 342.00 |
| 0.8290 | 342.00 |
| 0.8640 | 342.00 |
| 0.9540 | 342.00 |
Operational condition: Pressure, kPa = 101.4 (Gas)
| Mole fraction of n-Hexane (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0390 | 355.80 |
| 0.1520 | 351.70 |
| 0.2390 | 349.00 |
| 0.3330 | 347.00 |
| 0.4630 | 344.90 |
| 0.5810 | 343.70 |
| 0.6670 | 343.00 |
| 0.7310 | 342.60 |
| 0.7750 | 342.30 |
| 0.7950 | 342.10 |
| 0.8020 | 342.10 |
| 0.8080 | 342.00 |
| 0.8290 | 342.00 |
| 0.8640 | 342.00 |
| 0.9540 | 342.00 |