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 = 332.95 K
x (mol mol-1) x (mol mol-1)
0.0297 0.4328
0.3230 0.8762
0.3601 0.889
0.4016 0.9044
0.4400 0.9125
0.4781 0.9199
0.5288 0.9281
0.5757 0.9383
0.6306 0.9438
0.6791 0.9526
0.7308 0.9577
0.0598 0.592
0.7795 0.9669
0.8298 0.9731
0.8783 0.9809
0.9279 0.989
0.9788 0.9972
0.0901 0.6961
0.1010 0.7182
0.1200 0.7473
0.1592 0.7931
0.1993 0.8242
0.2395 0.8445
0.2803 0.8659
30882; 3-methylbutan-1-ol + ethyl acetate; 00019:00447