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 |