Operational condition: Pressure, kPa = 100 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2-Butanone (2) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of 2-Butanone (2) - Liquid mixture 1 |
293.15 | 0.0000 | 0.9986 | 0.0655 | 0.0000 |
293.15 | 0.0054 | 0.9928 | 0.0784 | 0.1229 |
293.15 | 0.0339 | 0.9645 | 0.1623 | 0.5590 |
293.15 | 0.0087 | 0.9897 | 0.0929 | 0.1746 |
293.15 | 0.0355 | 0.9632 | 0.1712 | 0.5811 |
293.15 | 0.0124 | 0.9860 | 0.1053 | 0.2519 |
293.15 | 0.0885 | 0.9115 | 0.3209 | 0.6791 |
293.15 | 0.0158 | 0.9831 | 0.1068 | 0.3139 |
293.15 | 0.0188 | 0.9801 | 0.1134 | 0.3845 |
293.15 | 0.0222 | 0.9765 | 0.1311 | 0.4380 |
293.15 | 0.0241 | 0.9748 | 0.1380 | 0.4922 |
293.15 | 0.0286 | 0.9703 | 0.1477 | 0.5332 |
298.15 | 0.0170 | 0.9817 | 0.1199 | 0.3914 |
298.15 | 0.0239 | 0.9749 | 0.1530 | 0.4851 |
298.15 | 0.0279 | 0.9707 | 0.1572 | 0.5261 |
298.15 | 0.0303 | 0.9684 | 0.1631 | 0.5582 |
298.15 | 0.0320 | 0.9671 | 0.1832 | 0.5791 |
298.15 | 0.0774 | 0.9226 | 0.3164 | 0.6836 |
298.15 | 0.0202 | 0.9785 | 0.1344 | 0.4402 |
298.15 | 0.0000 | 0.9985 | 0.0720 | 0.0000 |
298.15 | 0.0044 | 0.9938 | 0.0887 | 0.1103 |
298.15 | 0.0077 | 0.9907 | 0.0999 | 0.1965 |
298.15 | 0.0114 | 0.9870 | 0.1098 | 0.2634 |
298.15 | 0.0139 | 0.9846 | 0.1107 | 0.3220 |
303.15 | 0.0125 | 0.9862 | 0.1168 | 0.3180 |
303.15 | 0.0080 | 0.9909 | 0.1016 | 0.1970 |
303.15 | 0.0137 | 0.9852 | 0.1235 | 0.3962 |
303.15 | 0.0195 | 0.9792 | 0.1347 | 0.4427 |
303.15 | 0.0000 | 0.9982 | 0.0747 | 0.0000 |
303.15 | 0.0039 | 0.9945 | 0.0891 | 0.1182 |
303.15 | 0.0223 | 0.9764 | 0.1541 | 0.4857 |
303.15 | 0.0255 | 0.9733 | 0.1554 | 0.5310 |
303.15 | 0.0293 | 0.9696 | 0.1702 | 0.5556 |
303.15 | 0.0313 | 0.9677 | 0.1844 | 0.5771 |
303.15 | 0.0100 | 0.9884 | 0.1120 | 0.2635 |
303.15 | 0.0688 | 0.9312 | 0.3273 | 0.6727 |
313.15 | 0.0282 | 0.9710 | 0.1976 | 0.5730 |
313.15 | 0.0648 | 0.9352 | 0.3220 | 0.6780 |
313.15 | 0.0061 | 0.9929 | 0.1038 | 0.1972 |
313.15 | 0.0000 | 0.9986 | 0.0851 | 0.0000 |
313.15 | 0.0100 | 0.9884 | 0.1020 | 0.2765 |
313.15 | 0.0118 | 0.9868 | 0.1119 | 0.3296 |
313.15 | 0.0154 | 0.9832 | 0.1275 | 0.3985 |
313.15 | 0.0165 | 0.9827 | 0.1353 | 0.4470 |
313.15 | 0.0208 | 0.9779 | 0.1551 | 0.4871 |
313.15 | 0.0032 | 0.9958 | 0.0924 | 0.1181 |
313.15 | 0.0226 | 0.9766 | 0.1631 | 0.5289 |
313.15 | 0.0244 | 0.9749 | 0.1781 | 0.5523 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2-Butanone (2) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of 2-Butanone (2) - Liquid mixture 1 |
293.15 | 0.0000 | 0.9986 | 0.0655 | 0.0000 |
293.15 | 0.0054 | 0.9928 | 0.0784 | 0.1229 |
293.15 | 0.0339 | 0.9645 | 0.1623 | 0.5590 |
293.15 | 0.0087 | 0.9897 | 0.0929 | 0.1746 |
293.15 | 0.0355 | 0.9632 | 0.1712 | 0.5811 |
293.15 | 0.0124 | 0.9860 | 0.1053 | 0.2519 |
293.15 | 0.0885 | 0.9115 | 0.3209 | 0.6791 |
293.15 | 0.0158 | 0.9831 | 0.1068 | 0.3139 |
293.15 | 0.0188 | 0.9801 | 0.1134 | 0.3845 |
293.15 | 0.0222 | 0.9765 | 0.1311 | 0.4380 |
293.15 | 0.0241 | 0.9748 | 0.1380 | 0.4922 |
293.15 | 0.0286 | 0.9703 | 0.1477 | 0.5332 |
298.15 | 0.0170 | 0.9817 | 0.1199 | 0.3914 |
298.15 | 0.0239 | 0.9749 | 0.1530 | 0.4851 |
298.15 | 0.0279 | 0.9707 | 0.1572 | 0.5261 |
298.15 | 0.0303 | 0.9684 | 0.1631 | 0.5582 |
298.15 | 0.0320 | 0.9671 | 0.1832 | 0.5791 |
298.15 | 0.0774 | 0.9226 | 0.3164 | 0.6836 |
298.15 | 0.0202 | 0.9785 | 0.1344 | 0.4402 |
298.15 | 0.0000 | 0.9985 | 0.0720 | 0.0000 |
298.15 | 0.0044 | 0.9938 | 0.0887 | 0.1103 |
298.15 | 0.0077 | 0.9907 | 0.0999 | 0.1965 |
298.15 | 0.0114 | 0.9870 | 0.1098 | 0.2634 |
298.15 | 0.0139 | 0.9846 | 0.1107 | 0.3220 |
303.15 | 0.0125 | 0.9862 | 0.1168 | 0.3180 |
303.15 | 0.0080 | 0.9909 | 0.1016 | 0.1970 |
303.15 | 0.0137 | 0.9852 | 0.1235 | 0.3962 |
303.15 | 0.0195 | 0.9792 | 0.1347 | 0.4427 |
303.15 | 0.0000 | 0.9982 | 0.0747 | 0.0000 |
303.15 | 0.0039 | 0.9945 | 0.0891 | 0.1182 |
303.15 | 0.0223 | 0.9764 | 0.1541 | 0.4857 |
303.15 | 0.0255 | 0.9733 | 0.1554 | 0.5310 |
303.15 | 0.0293 | 0.9696 | 0.1702 | 0.5556 |
303.15 | 0.0313 | 0.9677 | 0.1844 | 0.5771 |
303.15 | 0.0100 | 0.9884 | 0.1120 | 0.2635 |
303.15 | 0.0688 | 0.9312 | 0.3273 | 0.6727 |
313.15 | 0.0282 | 0.9710 | 0.1976 | 0.5730 |
313.15 | 0.0648 | 0.9352 | 0.3220 | 0.6780 |
313.15 | 0.0061 | 0.9929 | 0.1038 | 0.1972 |
313.15 | 0.0000 | 0.9986 | 0.0851 | 0.0000 |
313.15 | 0.0100 | 0.9884 | 0.1020 | 0.2765 |
313.15 | 0.0118 | 0.9868 | 0.1119 | 0.3296 |
313.15 | 0.0154 | 0.9832 | 0.1275 | 0.3985 |
313.15 | 0.0165 | 0.9827 | 0.1353 | 0.4470 |
313.15 | 0.0208 | 0.9779 | 0.1551 | 0.4871 |
313.15 | 0.0032 | 0.9958 | 0.0924 | 0.1181 |
313.15 | 0.0226 | 0.9766 | 0.1631 | 0.5289 |
313.15 | 0.0244 | 0.9749 | 0.1781 | 0.5523 |