Operational condition: Pressure, kPa = 100 (Liquid)
Mole fraction of n-Hexane (1) - Liquid | Mole fraction of n-Hexane (1) - Gas |
---|---|
0.0150 | 0.0850 |
0.0380 | 0.1920 |
0.0980 | 0.3980 |
0.1480 | 0.5170 |
0.1950 | 0.5960 |
0.2510 | 0.6710 |
0.2940 | 0.7090 |
0.3730 | 0.7780 |
0.4180 | 0.8040 |
0.4720 | 0.8320 |
0.5200 | 0.8520 |
0.5730 | 0.8730 |
0.6330 | 0.8910 |
0.6820 | 0.9050 |
0.7300 | 0.9210 |
0.7830 | 0.9350 |
0.8330 | 0.9470 |
0.8780 | 0.9630 |
0.9250 | 0.9780 |
0.9540 | 0.9870 |
Operational condition: Pressure, kPa = 100 (Liquid)
Mole fraction of n-Hexane (1) - Liquid | Mole fraction of n-Hexane (1) - Gas |
---|---|
0.0150 | 0.0850 |
0.0380 | 0.1920 |
0.0980 | 0.3980 |
0.1480 | 0.5170 |
0.1950 | 0.5960 |
0.2510 | 0.6710 |
0.2940 | 0.7090 |
0.3730 | 0.7780 |
0.4180 | 0.8040 |
0.4720 | 0.8320 |
0.5200 | 0.8520 |
0.5730 | 0.8730 |
0.6330 | 0.8910 |
0.6820 | 0.9050 |
0.7300 | 0.9210 |
0.7830 | 0.9350 |
0.8330 | 0.9470 |
0.8780 | 0.9630 |
0.9250 | 0.9780 |
0.9540 | 0.9870 |
Operational condition: Pressure, kPa = 100 (Liquid)
Mole fraction of n-Hexane (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0150 | 391.29 |
0.0380 | 388.09 |
0.0980 | 380.32 |
0.1480 | 375.04 |
0.1950 | 371.15 |
0.2510 | 366.84 |
0.2940 | 364.07 |
0.3730 | 359.85 |
0.4180 | 357.90 |
0.4720 | 355.64 |
0.5200 | 353.83 |
0.5730 | 352.05 |
0.6330 | 350.37 |
0.6820 | 349.07 |
0.7300 | 347.72 |
0.7830 | 346.41 |
0.8330 | 345.27 |
0.8780 | 344.13 |
0.9250 | 343.07 |
0.9540 | 342.44 |
Operational condition: Pressure, kPa = 100 (Liquid)
Mole fraction of n-Hexane (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0150 | 391.29 |
0.0380 | 388.09 |
0.0980 | 380.32 |
0.1480 | 375.04 |
0.1950 | 371.15 |
0.2510 | 366.84 |
0.2940 | 364.07 |
0.3730 | 359.85 |
0.4180 | 357.90 |
0.4720 | 355.64 |
0.5200 | 353.83 |
0.5730 | 352.05 |
0.6330 | 350.37 |
0.6820 | 349.07 |
0.7300 | 347.72 |
0.7830 | 346.41 |
0.8330 | 345.27 |
0.8780 | 344.13 |
0.9250 | 343.07 |
0.9540 | 342.44 |