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) Tbp (K)
0 407.95
0.500 381.9
0.557 380.03
0.611 378.49
0.662 377.06
0.713 375.74
0.760 374.62
0.806 373.57
0.852 372.57
0.897 371.74
0.937 371.05
0.043 404.5
0.974 370.42
1 369.75
0.095 400.89
0.152 397.27
0.211 393.97
0.264 391.23
0.321 388.57
0.378 386.18
0.439 383.92
30588; propan-1-ol + 2-ethoxyethan-1-ol; 00056:00101