Isobaric Vapor-Liquid Equilibria for Three Ternary Systems: Water + 2-Propanol + 1-Ethyl-3-methylimidazolium Tetrafluoroborate, Water + 1-Propanol + 1-Ethyl-3-methylimidazolium Tetrafluoroborate, and Water + 1-Propanol + 1-Butyl-3-methylimidazolium Tetrafluoroborate Zhang, L.; Han, J.; Wang, R.; Qiu, X.; Ji, J.; Journal of Chemical & Engineering Data 2007, 52, 1401-1407
Data
P = 100 kPa
x (mol mol-1) x (mol mol-1) x (mol mol-1)
0.0016 0.8302 0.9981
0.0462 0.4231 0.9697
0.0499 0.8390 0.943
0.0612 0.6394 0.9476
0.0750 0.4054 0.95
0.0837 0.7579 0.9125
0.1010 0.7920 0.8914
0.1064 0.6040 0.9103
0.1121 0.3825 0.9216
0.1272 0.7195 0.8767
0.1536 0.3570 0.8928
0.0066 0.6820 0.9942
0.1584 0.7392 0.8435
0.1700 0.6817 0.8433
0.1705 0.5540 0.867
0.2060 0.3248 0.8555
0.2171 0.6402 0.8108
0.2182 0.6843 0.7966
0.2415 0.4985 0.8192
0.2682 0.5951 0.7794
0.2786 0.2800 0.7963
0.2929 0.6156 0.7498
0.0088 0.4462 0.9946
0.3119 0.5566 0.755
0.3271 0.4317 0.7606
0.3502 0.2359 0.746
0.3527 0.5206 0.7286
0.3714 0.5435 0.7105
0.3893 0.4882 0.7096
0.4180 0.3607 0.7187
0.4325 0.1852 0.6857
0.4654 0.4570 0.6673
0.4756 0.4121 0.6781
0.0108 0.8750 0.9869
0.5033 0.2941 0.6787
0.5259 0.1275 0.5885
0.5654 0.3329 0.6424
0.5656 0.3649 0.6397
0.5764 0.0964 0.5461
0.6209 0.2022 0.637
0.6632 0.2466 0.6179
0.6671 0.2715 0.6219
0.7077 0.1344 0.61
0.7453 0.1050 0.5751
0.0167 0.8169 0.9811
0.7663 0.1557 0.5971
0.7729 0.1742 0.5917
0.8252 0.1037 0.5786
0.8420 0.1108 0.573
0.0224 0.6697 0.9806
0.0238 0.4369 0.9846
0.0378 0.8501 0.9559
0.0414 0.7952 0.9549
24486; propan-2-ol + water + 1-ethyl-3-methylimidazolium tetrafluoroborate; 00004:00082:00322