Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of Butanoic acid (1) - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Butanoic acid (1) - Liquid mixture 2 |
298.15 | 0.9740 | 0.0233 | 0.0230 | 0.1406 |
298.15 | 0.9607 | 0.0364 | 0.0338 | 0.2284 |
298.15 | 0.9483 | 0.0486 | 0.0452 | 0.2994 |
298.15 | 0.9398 | 0.0569 | 0.0648 | 0.3834 |
298.15 | 0.9220 | 0.0706 | 0.0842 | 0.4414 |
298.15 | 0.9130 | 0.0794 | 0.1024 | 0.4933 |
298.15 | 0.9046 | 0.0876 | 0.1148 | 0.5358 |
298.15 | 0.8961 | 0.0959 | 0.1320 | 0.5778 |
308.15 | 0.9764 | 0.0233 | 0.0175 | 0.1247 |
308.15 | 0.9630 | 0.0364 | 0.0263 | 0.2172 |
308.15 | 0.9507 | 0.0485 | 0.0496 | 0.3072 |
308.15 | 0.9430 | 0.0558 | 0.0598 | 0.3552 |
308.15 | 0.9302 | 0.0683 | 0.0734 | 0.4331 |
308.15 | 0.9178 | 0.0798 | 0.0851 | 0.4871 |
308.15 | 0.9140 | 0.0834 | 0.1069 | 0.5418 |
308.15 | 0.8973 | 0.0999 | 0.1306 | 0.5771 |
318.15 | 0.9775 | 0.0220 | 0.0354 | 0.1157 |
318.15 | 0.9626 | 0.0340 | 0.0527 | 0.2008 |
318.15 | 0.9488 | 0.0468 | 0.0629 | 0.2842 |
318.15 | 0.9405 | 0.0543 | 0.0701 | 0.3351 |
318.15 | 0.9280 | 0.0666 | 0.0917 | 0.4438 |
318.15 | 0.9165 | 0.0769 | 0.1135 | 0.4770 |
318.15 | 0.8879 | 0.1045 | 0.1387 | 0.5168 |
318.15 | 0.8735 | 0.1179 | 0.1685 | 0.5480 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of Butanoic acid (1) - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Butanoic acid (1) - Liquid mixture 2 |
298.15 | 0.9740 | 0.0233 | 0.0230 | 0.1406 |
298.15 | 0.9607 | 0.0364 | 0.0338 | 0.2284 |
298.15 | 0.9483 | 0.0486 | 0.0452 | 0.2994 |
298.15 | 0.9398 | 0.0569 | 0.0648 | 0.3834 |
298.15 | 0.9220 | 0.0706 | 0.0842 | 0.4414 |
298.15 | 0.9130 | 0.0794 | 0.1024 | 0.4933 |
298.15 | 0.9046 | 0.0876 | 0.1148 | 0.5358 |
298.15 | 0.8961 | 0.0959 | 0.1320 | 0.5778 |
308.15 | 0.9764 | 0.0233 | 0.0175 | 0.1247 |
308.15 | 0.9630 | 0.0364 | 0.0263 | 0.2172 |
308.15 | 0.9507 | 0.0485 | 0.0496 | 0.3072 |
308.15 | 0.9430 | 0.0558 | 0.0598 | 0.3552 |
308.15 | 0.9302 | 0.0683 | 0.0734 | 0.4331 |
308.15 | 0.9178 | 0.0798 | 0.0851 | 0.4871 |
308.15 | 0.9140 | 0.0834 | 0.1069 | 0.5418 |
308.15 | 0.8973 | 0.0999 | 0.1306 | 0.5771 |
318.15 | 0.9775 | 0.0220 | 0.0354 | 0.1157 |
318.15 | 0.9626 | 0.0340 | 0.0527 | 0.2008 |
318.15 | 0.9488 | 0.0468 | 0.0629 | 0.2842 |
318.15 | 0.9405 | 0.0543 | 0.0701 | 0.3351 |
318.15 | 0.9280 | 0.0666 | 0.0917 | 0.4438 |
318.15 | 0.9165 | 0.0769 | 0.1135 | 0.4770 |
318.15 | 0.8879 | 0.1045 | 0.1387 | 0.5168 |
318.15 | 0.8735 | 0.1179 | 0.1685 | 0.5480 |