Isothermal vapor-liquid equilibria for different binary mixtures involved in the alcoholic distillation Sanz, M.T.; Gmehling, J.; Fluid Phase Equilibria 2008, 267, 158-162
Data
T = 332.7 K, P = 101 kPa
x (mol mol-1) ρ (kg m-3)
0 778.14
0.5339 812.5
0.5891 816.6
0.6597 821.96
0.7088 825.91
0.7693 830.72
0.8286 835.79
0.8882 840.96
0.9488 846.43
1 851.36
0.0501 780.94
0.1087 784.25
0.1714 788.1
0.2296 791.81
0.2900 795.6
0.3561 799.89
0.4088 803.56
0.4659 807.59
30882; 3-methylbutan-1-ol + ethyl acetate; 00019:00447