Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Mole fraction of 1-Propanol, 2-methyl- (2) - Gas |
---|---|
0.9490 | 0.9400 |
0.9130 | 0.9010 |
0.8790 | 0.8670 |
0.8450 | 0.8350 |
0.8090 | 0.8020 |
0.7760 | 0.7740 |
0.7280 | 0.7330 |
0.6850 | 0.6970 |
0.6400 | 0.6600 |
0.6180 | 0.6430 |
0.5630 | 0.5970 |
0.5050 | 0.5500 |
0.4450 | 0.4990 |
0.3920 | 0.4510 |
0.3330 | 0.3950 |
0.2810 | 0.3440 |
0.2030 | 0.2610 |
0.1230 | 0.1660 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Mole fraction of 1-Propanol, 2-methyl- (2) - Gas |
---|---|
0.9490 | 0.9400 |
0.9130 | 0.9010 |
0.8790 | 0.8670 |
0.8450 | 0.8350 |
0.8090 | 0.8020 |
0.7760 | 0.7740 |
0.7280 | 0.7330 |
0.6850 | 0.6970 |
0.6400 | 0.6600 |
0.6180 | 0.6430 |
0.5630 | 0.5970 |
0.5050 | 0.5500 |
0.4450 | 0.4990 |
0.3920 | 0.4510 |
0.3330 | 0.3950 |
0.2810 | 0.3440 |
0.2030 | 0.2610 |
0.1230 | 0.1660 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.9490 | 380.38 |
0.9130 | 380.22 |
0.8790 | 380.11 |
0.8450 | 380.03 |
0.8090 | 379.98 |
0.7760 | 379.97 |
0.7280 | 379.98 |
0.6850 | 380.02 |
0.6400 | 380.09 |
0.6180 | 380.12 |
0.5630 | 380.25 |
0.5050 | 380.45 |
0.4450 | 380.71 |
0.3920 | 380.98 |
0.3330 | 381.35 |
0.2810 | 381.74 |
0.2030 | 382.40 |
0.1230 | 383.23 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.9490 | 380.38 |
0.9130 | 380.22 |
0.8790 | 380.11 |
0.8450 | 380.03 |
0.8090 | 379.98 |
0.7760 | 379.97 |
0.7280 | 379.98 |
0.6850 | 380.02 |
0.6400 | 380.09 |
0.6180 | 380.12 |
0.5630 | 380.25 |
0.5050 | 380.45 |
0.4450 | 380.71 |
0.3920 | 380.98 |
0.3330 | 381.35 |
0.2810 | 381.74 |
0.2030 | 382.40 |
0.1230 | 383.23 |