Operational condition: Pressure, kPa = 101.3 (Gas)
| Mole fraction of Acetic acid, trifluoro-, ethyl ester (2) - Liquid | Mole fraction of Acetic acid, trifluoro-, ethyl ester (2) - Gas |
|---|---|
| 1.0000 | 1.0000 |
| 0.9916 | 0.9935 |
| 0.9685 | 0.9540 |
| 0.9398 | 0.9064 |
| 0.8888 | 0.8521 |
| 0.8586 | 0.8395 |
| 0.8178 | 0.7984 |
| 0.7228 | 0.7711 |
| 0.6423 | 0.7460 |
| 0.4711 | 0.7103 |
| 0.4081 | 0.6930 |
| 0.3424 | 0.6703 |
| 0.3028 | 0.6631 |
| 0.2537 | 0.6305 |
| 0.2222 | 0.6179 |
| 0.1815 | 0.5745 |
| 0.1561 | 0.5482 |
| 0.1420 | 0.5271 |
| 0.1240 | 0.4930 |
| 0.0964 | 0.4501 |
| 0.0874 | 0.4222 |
| 0.0716 | 0.3871 |
| 0.0632 | 0.3536 |
| 0.0414 | 0.3080 |
| 0.0406 | 0.2741 |
| 0.0323 | 0.2359 |
| 0.0264 | 0.2130 |
| 0.0210 | 0.1764 |
| 0.0180 | 0.1281 |
| 0.0091 | 0.0930 |
| 0.0045 | 0.0500 |
| 0.0000 | 0.0000 |
Operational condition: Pressure, kPa = 101.3 (Gas)
| Mole fraction of Acetic acid, trifluoro-, ethyl ester (2) - Liquid | Mole fraction of Acetic acid, trifluoro-, ethyl ester (2) - Gas |
|---|---|
| 1.0000 | 1.0000 |
| 0.9916 | 0.9935 |
| 0.9685 | 0.9540 |
| 0.9398 | 0.9064 |
| 0.8888 | 0.8521 |
| 0.8586 | 0.8395 |
| 0.8178 | 0.7984 |
| 0.7228 | 0.7711 |
| 0.6423 | 0.7460 |
| 0.4711 | 0.7103 |
| 0.4081 | 0.6930 |
| 0.3424 | 0.6703 |
| 0.3028 | 0.6631 |
| 0.2537 | 0.6305 |
| 0.2222 | 0.6179 |
| 0.1815 | 0.5745 |
| 0.1561 | 0.5482 |
| 0.1420 | 0.5271 |
| 0.1240 | 0.4930 |
| 0.0964 | 0.4501 |
| 0.0874 | 0.4222 |
| 0.0716 | 0.3871 |
| 0.0632 | 0.3536 |
| 0.0414 | 0.3080 |
| 0.0406 | 0.2741 |
| 0.0323 | 0.2359 |
| 0.0264 | 0.2130 |
| 0.0210 | 0.1764 |
| 0.0180 | 0.1281 |
| 0.0091 | 0.0930 |
| 0.0045 | 0.0500 |
| 0.0000 | 0.0000 |
Operational condition: Pressure, kPa = 101.3 (Gas)
| Mole fraction of Acetic acid, trifluoro-, ethyl ester (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 1.0000 | 335.67 |
| 0.9916 | 334.77 |
| 0.9685 | 333.77 |
| 0.9398 | 332.46 |
| 0.8888 | 331.47 |
| 0.8586 | 331.08 |
| 0.8178 | 330.78 |
| 0.7228 | 330.56 |
| 0.6423 | 330.65 |
| 0.4711 | 331.49 |
| 0.4081 | 331.93 |
| 0.3424 | 332.46 |
| 0.3028 | 332.97 |
| 0.2537 | 333.74 |
| 0.2222 | 334.34 |
| 0.1815 | 335.55 |
| 0.1561 | 336.35 |
| 0.1420 | 336.72 |
| 0.1240 | 338.15 |
| 0.0964 | 339.27 |
| 0.0874 | 340.13 |
| 0.0716 | 341.35 |
| 0.0632 | 342.36 |
| 0.0414 | 343.85 |
| 0.0406 | 344.74 |
| 0.0323 | 345.93 |
| 0.0264 | 346.75 |
| 0.0210 | 347.60 |
| 0.0180 | 348.53 |
| 0.0091 | 349.50 |
| 0.0045 | 350.50 |
| 0.0000 | 351.55 |
Operational condition: Pressure, kPa = 101.3 (Gas)
| Mole fraction of Acetic acid, trifluoro-, ethyl ester (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 1.0000 | 335.67 |
| 0.9916 | 334.77 |
| 0.9685 | 333.77 |
| 0.9398 | 332.46 |
| 0.8888 | 331.47 |
| 0.8586 | 331.08 |
| 0.8178 | 330.78 |
| 0.7228 | 330.56 |
| 0.6423 | 330.65 |
| 0.4711 | 331.49 |
| 0.4081 | 331.93 |
| 0.3424 | 332.46 |
| 0.3028 | 332.97 |
| 0.2537 | 333.74 |
| 0.2222 | 334.34 |
| 0.1815 | 335.55 |
| 0.1561 | 336.35 |
| 0.1420 | 336.72 |
| 0.1240 | 338.15 |
| 0.0964 | 339.27 |
| 0.0874 | 340.13 |
| 0.0716 | 341.35 |
| 0.0632 | 342.36 |
| 0.0414 | 343.85 |
| 0.0406 | 344.74 |
| 0.0323 | 345.93 |
| 0.0264 | 346.75 |
| 0.0210 | 347.60 |
| 0.0180 | 348.53 |
| 0.0091 | 349.50 |
| 0.0045 | 350.50 |
| 0.0000 | 351.55 |