Operational condition: Pressure, kPa = 101.33 (Gas)
| Mole fraction of Thiophene, 2-ethyl- (2) - Liquid | Mole fraction of Thiophene, 2-ethyl- (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0645 | 0.2031 |
| 0.0915 | 0.2697 |
| 0.1153 | 0.3218 |
| 0.1400 | 0.3704 |
| 0.1613 | 0.4084 |
| 0.1762 | 0.4330 |
| 0.2055 | 0.4776 |
| 0.2479 | 0.5343 |
| 0.3659 | 0.6563 |
| 0.4602 | 0.7286 |
| 0.5084 | 0.7597 |
| 0.5861 | 0.8040 |
| 0.6465 | 0.8346 |
| 0.7028 | 0.8610 |
| 0.7776 | 0.8943 |
| 0.8442 | 0.9234 |
| 0.9231 | 0.9596 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.33 (Gas)
| Mole fraction of Thiophene, 2-ethyl- (2) - Liquid | Mole fraction of Thiophene, 2-ethyl- (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0645 | 0.2031 |
| 0.0915 | 0.2697 |
| 0.1153 | 0.3218 |
| 0.1400 | 0.3704 |
| 0.1613 | 0.4084 |
| 0.1762 | 0.4330 |
| 0.2055 | 0.4776 |
| 0.2479 | 0.5343 |
| 0.3659 | 0.6563 |
| 0.4602 | 0.7286 |
| 0.5084 | 0.7597 |
| 0.5861 | 0.8040 |
| 0.6465 | 0.8346 |
| 0.7028 | 0.8610 |
| 0.7776 | 0.8943 |
| 0.8442 | 0.9234 |
| 0.9231 | 0.9596 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of Thiophene, 2-ethyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 447.46 |
| 0.0645 | 440.89 |
| 0.0915 | 438.56 |
| 0.1153 | 436.67 |
| 0.1400 | 434.84 |
| 0.1613 | 433.37 |
| 0.1762 | 432.39 |
| 0.2055 | 430.58 |
| 0.2479 | 428.18 |
| 0.3659 | 422.66 |
| 0.4602 | 419.17 |
| 0.5084 | 417.62 |
| 0.5861 | 415.40 |
| 0.6465 | 413.88 |
| 0.7028 | 412.59 |
| 0.7776 | 411.03 |
| 0.8442 | 409.77 |
| 0.9231 | 408.39 |
| 1.0000 | 407.14 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of Thiophene, 2-ethyl- (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 447.46 |
| 0.0645 | 440.89 |
| 0.0915 | 438.56 |
| 0.1153 | 436.67 |
| 0.1400 | 434.84 |
| 0.1613 | 433.37 |
| 0.1762 | 432.39 |
| 0.2055 | 430.58 |
| 0.2479 | 428.18 |
| 0.3659 | 422.66 |
| 0.4602 | 419.17 |
| 0.5084 | 417.62 |
| 0.5861 | 415.40 |
| 0.6465 | 413.88 |
| 0.7028 | 412.59 |
| 0.7776 | 411.03 |
| 0.8442 | 409.77 |
| 0.9231 | 408.39 |
| 1.0000 | 407.14 |