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 |
|---|---|
| 0.0000 | 0.0000 |
| 0.0570 | 0.1490 |
| 0.1040 | 0.2580 |
| 0.1640 | 0.3850 |
| 0.2260 | 0.4900 |
| 0.2750 | 0.5670 |
| 0.3280 | 0.6390 |
| 0.3850 | 0.7050 |
| 0.4460 | 0.7580 |
| 0.4940 | 0.8000 |
| 0.5440 | 0.8360 |
| 0.6020 | 0.8640 |
| 0.6540 | 0.8910 |
| 0.7090 | 0.9240 |
| 0.7590 | 0.9410 |
| 0.8080 | 0.9560 |
| 0.8510 | 0.9690 |
| 0.8950 | 0.9790 |
| 0.9370 | 0.9880 |
| 1.0000 | 1.0000 |
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 |
|---|---|
| 0.0000 | 0.0000 |
| 0.0570 | 0.1490 |
| 0.1040 | 0.2580 |
| 0.1640 | 0.3850 |
| 0.2260 | 0.4900 |
| 0.2750 | 0.5670 |
| 0.3280 | 0.6390 |
| 0.3850 | 0.7050 |
| 0.4460 | 0.7580 |
| 0.4940 | 0.8000 |
| 0.5440 | 0.8360 |
| 0.6020 | 0.8640 |
| 0.6540 | 0.8910 |
| 0.7090 | 0.9240 |
| 0.7590 | 0.9410 |
| 0.8080 | 0.9560 |
| 0.8510 | 0.9690 |
| 0.8950 | 0.9790 |
| 0.9370 | 0.9880 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 425.63 |
| 0.0570 | 421.95 |
| 0.1040 | 418.45 |
| 0.1640 | 414.98 |
| 0.2260 | 411.65 |
| 0.2750 | 408.99 |
| 0.3280 | 405.92 |
| 0.3850 | 403.28 |
| 0.4460 | 400.58 |
| 0.4940 | 398.11 |
| 0.5440 | 395.95 |
| 0.6020 | 393.97 |
| 0.6540 | 391.86 |
| 0.7090 | 389.26 |
| 0.7590 | 387.69 |
| 0.8080 | 385.97 |
| 0.8510 | 384.64 |
| 0.8950 | 383.20 |
| 0.9370 | 382.06 |
| 1.0000 | 381.09 |
Operational condition: Pressure, kPa = 95.5 (Liquid)
| Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 421.15 |
| 0.0512 | 417.45 |
| 0.0890 | 414.95 |
| 0.1501 | 411.45 |
| 0.1918 | 408.55 |
| 0.2510 | 405.45 |
| 0.2952 | 403.45 |
| 0.3501 | 400.55 |
| 0.4111 | 397.75 |
| 0.4501 | 396.15 |
| 0.5013 | 394.25 |
| 0.5502 | 392.25 |
| 0.6185 | 389.35 |
| 0.6503 | 388.85 |
| 0.7050 | 387.15 |
| 0.7502 | 385.75 |
| 0.8204 | 383.85 |
| 0.8501 | 383.15 |
| 0.8933 | 382.05 |
| 0.9502 | 380.75 |
| 1.0000 | 379.76 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 425.63 |
| 0.0570 | 421.95 |
| 0.1040 | 418.45 |
| 0.1640 | 414.98 |
| 0.2260 | 411.65 |
| 0.2750 | 408.99 |
| 0.3280 | 405.92 |
| 0.3850 | 403.28 |
| 0.4460 | 400.58 |
| 0.4940 | 398.11 |
| 0.5440 | 395.95 |
| 0.6020 | 393.97 |
| 0.6540 | 391.86 |
| 0.7090 | 389.26 |
| 0.7590 | 387.69 |
| 0.8080 | 385.97 |
| 0.8510 | 384.64 |
| 0.8950 | 383.20 |
| 0.9370 | 382.06 |
| 1.0000 | 381.09 |
Operational condition: Pressure, kPa = 95.5 (Liquid)
| Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 421.15 |
| 0.0512 | 417.45 |
| 0.0890 | 414.95 |
| 0.1501 | 411.45 |
| 0.1918 | 408.55 |
| 0.2510 | 405.45 |
| 0.2952 | 403.45 |
| 0.3501 | 400.55 |
| 0.4111 | 397.75 |
| 0.4501 | 396.15 |
| 0.5013 | 394.25 |
| 0.5502 | 392.25 |
| 0.6185 | 389.35 |
| 0.6503 | 388.85 |
| 0.7050 | 387.15 |
| 0.7502 | 385.75 |
| 0.8204 | 383.85 |
| 0.8501 | 383.15 |
| 0.8933 | 382.05 |
| 0.9502 | 380.75 |
| 1.0000 | 379.76 |