Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Liquid mixture 2 | Mole fraction of Ethyl Acetate (1) - Liquid mixture 2 | Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Liquid mixture 1 | Mole fraction of Ethyl Acetate (1) - Liquid mixture 1 |
298.15 | 0.0237 | 0.0023 | 0.3612 | 0.1501 |
298.15 | 0.0004 | 0.0097 | 0.0464 | 0.7608 |
298.15 | 0.0000 | 0.0139 | 0.0000 | 0.8285 |
298.15 | 0.0160 | 0.0034 | 0.3632 | 0.2326 |
298.15 | 0.0105 | 0.0036 | 0.3355 | 0.3127 |
298.15 | 0.0074 | 0.0040 | 0.2989 | 0.3839 |
298.15 | 0.0056 | 0.0053 | 0.2646 | 0.4426 |
298.15 | 0.0037 | 0.0066 | 0.2378 | 0.4867 |
298.15 | 0.0016 | 0.0076 | 0.1248 | 0.6619 |
298.15 | 0.0009 | 0.0087 | 0.0877 | 0.7139 |
298.15 | 0.0009 | 0.0095 | 0.0746 | 0.7286 |
318.15 | 0.0234 | 0.0026 | 0.3425 | 0.1457 |
318.15 | 0.0007 | 0.0093 | 0.0715 | 0.6989 |
318.15 | 0.0004 | 0.0097 | 0.0524 | 0.7240 |
318.15 | 0.0000 | 0.0117 | 0.0000 | 0.7946 |
318.15 | 0.0172 | 0.0033 | 0.3427 | 0.2206 |
318.15 | 0.0117 | 0.0044 | 0.3197 | 0.2920 |
318.15 | 0.0073 | 0.0052 | 0.2835 | 0.3742 |
318.15 | 0.0055 | 0.0054 | 0.2512 | 0.4371 |
318.15 | 0.0046 | 0.0065 | 0.2239 | 0.4843 |
318.15 | 0.0015 | 0.0073 | 0.1292 | 0.6243 |
318.15 | 0.0009 | 0.0078 | 0.0868 | 0.6805 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Liquid mixture 2 | Mole fraction of Ethyl Acetate (1) - Liquid mixture 2 | Mole fraction of 2,2,3,3-Tetrafluoro-1-propanol (2) - Liquid mixture 1 | Mole fraction of Ethyl Acetate (1) - Liquid mixture 1 |
298.15 | 0.0237 | 0.0023 | 0.3612 | 0.1501 |
298.15 | 0.0004 | 0.0097 | 0.0464 | 0.7608 |
298.15 | 0.0000 | 0.0139 | 0.0000 | 0.8285 |
298.15 | 0.0160 | 0.0034 | 0.3632 | 0.2326 |
298.15 | 0.0105 | 0.0036 | 0.3355 | 0.3127 |
298.15 | 0.0074 | 0.0040 | 0.2989 | 0.3839 |
298.15 | 0.0056 | 0.0053 | 0.2646 | 0.4426 |
298.15 | 0.0037 | 0.0066 | 0.2378 | 0.4867 |
298.15 | 0.0016 | 0.0076 | 0.1248 | 0.6619 |
298.15 | 0.0009 | 0.0087 | 0.0877 | 0.7139 |
298.15 | 0.0009 | 0.0095 | 0.0746 | 0.7286 |
318.15 | 0.0234 | 0.0026 | 0.3425 | 0.1457 |
318.15 | 0.0007 | 0.0093 | 0.0715 | 0.6989 |
318.15 | 0.0004 | 0.0097 | 0.0524 | 0.7240 |
318.15 | 0.0000 | 0.0117 | 0.0000 | 0.7946 |
318.15 | 0.0172 | 0.0033 | 0.3427 | 0.2206 |
318.15 | 0.0117 | 0.0044 | 0.3197 | 0.2920 |
318.15 | 0.0073 | 0.0052 | 0.2835 | 0.3742 |
318.15 | 0.0055 | 0.0054 | 0.2512 | 0.4371 |
318.15 | 0.0046 | 0.0065 | 0.2239 | 0.4843 |
318.15 | 0.0015 | 0.0073 | 0.1292 | 0.6243 |
318.15 | 0.0009 | 0.0078 | 0.0868 | 0.6805 |