Separation of azeotrope (2,2,3,3-tetrafluoro-1-propanol + water): Isobaric vapour-liquid phase equilibrium measurements and azeotropic distillation Shi, P.; Gao, Y.; Wu, J.; Xu, D.; Gao, J.; Ma, X.; Wang, Y.; The Journal of Chemical Thermodynamics 2017, 115, 19-26
Data
P = 101.3 kPa
x (mol mol-1) Tbp (K)
1 382.15
0.2090 386.66
0.1784 388.33
0.1471 390.7
0.1047 394.13
0.0852 396.75
0.0588 400.06
0.0438 402.55
0.0325 404.55
0.0212 406.87
0 411.45
0.9615 380.77
0.9268 379.77
0.8489 379.4
0.7218 379.45
0.5715 379.75
0.3708 381.95
0.3150 383.46
0.2530 385.18
46453; 2,2,3,3-tetrafluoro-1-propanol + 1,4-dimethylbenzene; 00202:00520