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 |