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)
0 334.35
0.7758 344.29
0.8372 347.6
0.8959 352.36
0.9059 353.77
0.9425 359.88
0.9517 362.39
0.9678 367.75
0.9805 371.3
0.9912 377.03
1 382.15
0.0296 334.23
0.0835 334.4
0.1562 334.83
0.2508 335.26
0.3644 336.04
0.4800 336.93
0.6353 339.43
0.7012 341.17
46452; 2,2,3,3-tetrafluoro-1-propanol + trichloromethane; 00021:00520