Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of Ethanol (1) - Liquid | Mole fraction of Ethanol (1) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0372 | 0.2148 |
| 0.0954 | 0.4000 |
| 0.1632 | 0.5251 |
| 0.2364 | 0.6084 |
| 0.2961 | 0.6575 |
| 0.3440 | 0.6858 |
| 0.3865 | 0.7078 |
| 0.4342 | 0.7271 |
| 0.4757 | 0.7442 |
| 0.5206 | 0.7603 |
| 0.5819 | 0.7825 |
| 0.6524 | 0.8062 |
| 0.7256 | 0.8325 |
| 0.7922 | 0.8606 |
| 0.8482 | 0.8862 |
| 0.8868 | 0.9076 |
| 0.9095 | 0.9213 |
| 0.9304 | 0.9360 |
| 0.9488 | 0.9507 |
| 0.9677 | 0.9663 |
| 0.9838 | 0.9822 |
| 0.9918 | 0.9908 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of Ethanol (1) - Liquid | Mole fraction of Ethanol (1) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0372 | 0.2148 |
| 0.0954 | 0.4000 |
| 0.1632 | 0.5251 |
| 0.2364 | 0.6084 |
| 0.2961 | 0.6575 |
| 0.3440 | 0.6858 |
| 0.3865 | 0.7078 |
| 0.4342 | 0.7271 |
| 0.4757 | 0.7442 |
| 0.5206 | 0.7603 |
| 0.5819 | 0.7825 |
| 0.6524 | 0.8062 |
| 0.7256 | 0.8325 |
| 0.7922 | 0.8606 |
| 0.8482 | 0.8862 |
| 0.8868 | 0.9076 |
| 0.9095 | 0.9213 |
| 0.9304 | 0.9360 |
| 0.9488 | 0.9507 |
| 0.9677 | 0.9663 |
| 0.9838 | 0.9822 |
| 0.9918 | 0.9908 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of Ethanol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 386.53 |
| 0.0372 | 379.97 |
| 0.0954 | 372.13 |
| 0.1632 | 366.94 |
| 0.2364 | 362.78 |
| 0.2961 | 359.96 |
| 0.3440 | 358.43 |
| 0.3865 | 357.31 |
| 0.4342 | 356.35 |
| 0.4757 | 355.62 |
| 0.5206 | 354.91 |
| 0.5819 | 354.10 |
| 0.6524 | 353.36 |
| 0.7256 | 352.69 |
| 0.7922 | 352.17 |
| 0.8482 | 351.85 |
| 0.8868 | 351.66 |
| 0.9095 | 351.58 |
| 0.9304 | 351.52 |
| 0.9488 | 351.47 |
| 0.9677 | 351.45 |
| 0.9838 | 351.47 |
| 0.9918 | 351.48 |
| 1.0000 | 351.50 |
Operational condition: Pressure, kPa = 101.33 (Liquid)
| Mole fraction of Ethanol (1) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 386.53 |
| 0.0372 | 379.97 |
| 0.0954 | 372.13 |
| 0.1632 | 366.94 |
| 0.2364 | 362.78 |
| 0.2961 | 359.96 |
| 0.3440 | 358.43 |
| 0.3865 | 357.31 |
| 0.4342 | 356.35 |
| 0.4757 | 355.62 |
| 0.5206 | 354.91 |
| 0.5819 | 354.10 |
| 0.6524 | 353.36 |
| 0.7256 | 352.69 |
| 0.7922 | 352.17 |
| 0.8482 | 351.85 |
| 0.8868 | 351.66 |
| 0.9095 | 351.58 |
| 0.9304 | 351.52 |
| 0.9488 | 351.47 |
| 0.9677 | 351.45 |
| 0.9838 | 351.47 |
| 0.9918 | 351.48 |
| 1.0000 | 351.50 |