Phase equilibria involved in extractive distillation of dipropyl ether + 1-propyl alcohol using 2-ethoxyethanol as entrainer Lladosa, E.; Montón, J.; Burguet, M.; Muñoz, R.; Fluid Phase Equilibria 2007, 255, 62-69
Data
P = 101.3 kPa
x (mol mol-1) x (mol mol-1)
0 0.0
0.500 0.787
0.557 0.824
0.611 0.854
0.662 0.878
0.713 0.901
0.760 0.922
0.806 0.94
0.852 0.956
0.897 0.969
0.937 0.982
0.043 0.138
0.974 0.992
1 1.0
0.095 0.267
0.152 0.391
0.211 0.486
0.264 0.562
0.321 0.632
0.378 0.689
0.439 0.746
30588; propan-1-ol + 2-ethoxyethan-1-ol; 00056:00101