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
0.361 373.34
0.413 371.78
0.463 370.77
0.520 369.67
0.576 368.51
0.635 367.5
0.690 366.68
0.765 365.76
0.823 365.0
0.877 364.36
0.029 400.36
0.937 363.63
1 363.16
0.066 393.98
0.100 389.46
0.140 385.26
0.180 382.04
0.228 379.28
0.268 377.06
0.311 375.07
30587; 2-ethoxyethan-1-ol + dipropyl ether; 00056:00580