Phase Equlibria for Hexyl Acetate Reactive Distillation Schmitt, M.; Hasse, H.; Journal of Chemical & Engineering Data 2005, 50, 1677-1683
Data
T = 413.15 K
x (mol mol-1) P (kPa)
0.0254 41.89
0.9125 57.23
0.9343 57.4
0.9566 57.45
0.9797 57.32
0.9894 57.18
0.0368 42.22
0.0655 43.08
0.0913 43.9
0.1175 44.7
0.2188 47.25
0.3225 49.67
0.4139 51.19
0.6003 54.71
4186; 1-hexanol + hexyl ethanoate; 00045:01104