Operational condition: Pressure, kPa = 40 (Liquid)
Mole fraction of 1-Hexanol, 2-ethyl- (2) - Liquid | Mole fraction of 1-Hexanol, 2-ethyl- (2) - Gas |
---|---|
0.0000 | 0.0000 |
0.0730 | 0.0840 |
0.1230 | 0.1410 |
0.1980 | 0.2250 |
0.2850 | 0.3270 |
0.3620 | 0.4200 |
0.4170 | 0.4920 |
0.4820 | 0.5710 |
0.5660 | 0.6680 |
0.6210 | 0.7350 |
0.7430 | 0.8530 |
0.8280 | 0.9150 |
0.8880 | 0.9540 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 40 (Liquid)
Mole fraction of 1-Hexanol, 2-ethyl- (2) - Liquid | Mole fraction of 1-Hexanol, 2-ethyl- (2) - Gas |
---|---|
0.0000 | 0.0000 |
0.0730 | 0.0840 |
0.1230 | 0.1410 |
0.1980 | 0.2250 |
0.2850 | 0.3270 |
0.3620 | 0.4200 |
0.4170 | 0.4920 |
0.4820 | 0.5710 |
0.5660 | 0.6680 |
0.6210 | 0.7350 |
0.7430 | 0.8530 |
0.8280 | 0.9150 |
0.8880 | 0.9540 |
1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 40 (Liquid)
Mole fraction of 1-Hexanol, 2-ethyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 441.80 |
0.0730 | 441.60 |
0.1230 | 441.40 |
0.1980 | 441.05 |
0.2850 | 440.35 |
0.3620 | 439.70 |
0.4170 | 439.10 |
0.4820 | 438.25 |
0.5660 | 436.75 |
0.6210 | 435.55 |
0.7430 | 432.90 |
0.8280 | 430.85 |
0.8880 | 429.55 |
1.0000 | 427.20 |
Operational condition: Pressure, kPa = 40 (Liquid)
Mole fraction of 1-Hexanol, 2-ethyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
---|---|
0.0000 | 441.80 |
0.0730 | 441.60 |
0.1230 | 441.40 |
0.1980 | 441.05 |
0.2850 | 440.35 |
0.3620 | 439.70 |
0.4170 | 439.10 |
0.4820 | 438.25 |
0.5660 | 436.75 |
0.6210 | 435.55 |
0.7430 | 432.90 |
0.8280 | 430.85 |
0.8880 | 429.55 |
1.0000 | 427.20 |