Operational condition: Temperature, K = 298.15 (Gas)
| Mole fraction of Ethanol, 2-methoxy- (1) - Liquid | Mole fraction of Ethanol, 2-methoxy- (1) - Gas |
|---|---|
| 0.0724 | 0.0159 |
| 0.1100 | 0.0223 |
| 0.1278 | 0.0282 |
| 0.1787 | 0.0392 |
| 0.1842 | 0.0405 |
| 0.2694 | 0.0626 |
| 0.3015 | 0.0704 |
| 0.3682 | 0.0916 |
| 0.4251 | 0.1164 |
| 0.4542 | 0.1231 |
| 0.5711 | 0.1821 |
| 0.6925 | 0.2584 |
| 0.7431 | 0.3173 |
| 0.8476 | 0.4552 |
| 0.9112 | 0.6015 |
| 0.9219 | 0.6215 |
| 0.9432 | 0.7044 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Ethanol (2) - Liquid | Mole fraction of Ethanol (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0520 | 0.2120 |
| 0.1010 | 0.3550 |
| 0.1500 | 0.4670 |
| 0.2080 | 0.5750 |
| 0.2640 | 0.6480 |
| 0.3130 | 0.7070 |
| 0.3650 | 0.7510 |
| 0.4230 | 0.7950 |
| 0.4850 | 0.8350 |
| 0.5370 | 0.8600 |
| 0.5890 | 0.8820 |
| 0.6400 | 0.9020 |
| 0.6960 | 0.9240 |
| 0.7500 | 0.9410 |
| 0.7990 | 0.9540 |
| 0.8580 | 0.9690 |
| 0.9020 | 0.9790 |
| 0.9440 | 0.9880 |
| 0.9790 | 0.9950 |
| 1.0000 | 1.0000 |
Operational condition: Temperature, K = 298.15 (Gas)
| Mole fraction of Ethanol, 2-methoxy- (1) - Liquid | Mole fraction of Ethanol, 2-methoxy- (1) - Gas |
|---|---|
| 0.0724 | 0.0159 |
| 0.1100 | 0.0223 |
| 0.1278 | 0.0282 |
| 0.1787 | 0.0392 |
| 0.1842 | 0.0405 |
| 0.2694 | 0.0626 |
| 0.3015 | 0.0704 |
| 0.3682 | 0.0916 |
| 0.4251 | 0.1164 |
| 0.4542 | 0.1231 |
| 0.5711 | 0.1821 |
| 0.6925 | 0.2584 |
| 0.7431 | 0.3173 |
| 0.8476 | 0.4552 |
| 0.9112 | 0.6015 |
| 0.9219 | 0.6215 |
| 0.9432 | 0.7044 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Ethanol (2) - Liquid | Mole fraction of Ethanol (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0520 | 0.2120 |
| 0.1010 | 0.3550 |
| 0.1500 | 0.4670 |
| 0.2080 | 0.5750 |
| 0.2640 | 0.6480 |
| 0.3130 | 0.7070 |
| 0.3650 | 0.7510 |
| 0.4230 | 0.7950 |
| 0.4850 | 0.8350 |
| 0.5370 | 0.8600 |
| 0.5890 | 0.8820 |
| 0.6400 | 0.9020 |
| 0.6960 | 0.9240 |
| 0.7500 | 0.9410 |
| 0.7990 | 0.9540 |
| 0.8580 | 0.9690 |
| 0.9020 | 0.9790 |
| 0.9440 | 0.9880 |
| 0.9790 | 0.9950 |
| 1.0000 | 1.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Ethanol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 397.58 |
| 0.0520 | 391.95 |
| 0.1010 | 387.48 |
| 0.1500 | 383.40 |
| 0.2080 | 379.16 |
| 0.2640 | 375.64 |
| 0.3130 | 372.83 |
| 0.3650 | 370.33 |
| 0.4230 | 367.65 |
| 0.4850 | 365.22 |
| 0.5370 | 363.42 |
| 0.5890 | 361.62 |
| 0.6400 | 360.20 |
| 0.6960 | 358.64 |
| 0.7500 | 357.32 |
| 0.7990 | 356.11 |
| 0.8580 | 354.78 |
| 0.9020 | 353.83 |
| 0.9440 | 353.07 |
| 0.9790 | 352.29 |
| 1.0000 | 351.91 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Ethanol (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 397.58 |
| 0.0520 | 391.95 |
| 0.1010 | 387.48 |
| 0.1500 | 383.40 |
| 0.2080 | 379.16 |
| 0.2640 | 375.64 |
| 0.3130 | 372.83 |
| 0.3650 | 370.33 |
| 0.4230 | 367.65 |
| 0.4850 | 365.22 |
| 0.5370 | 363.42 |
| 0.5890 | 361.62 |
| 0.6400 | 360.20 |
| 0.6960 | 358.64 |
| 0.7500 | 357.32 |
| 0.7990 | 356.11 |
| 0.8580 | 354.78 |
| 0.9020 | 353.83 |
| 0.9440 | 353.07 |
| 0.9790 | 352.29 |
| 1.0000 | 351.91 |