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
T (K) P (kPa)
345.63 9.97
373.00 30.94
375.49 33.97
378.51 37.93
381.26 41.98
383.78 45.88
386.12 49.91
388.87 54.89
391.39 59.83
393.83 64.82
396.01 69.65
349.72 11.98
398.10 74.57
400.12 79.47
402.11 84.74
403.97 89.84
405.76 94.91
407.95 101.3
353.30 13.98
356.42 15.98
359.27 17.98
363.08 20.96
365.34 22.97
367.46 24.98
370.33 27.95
100; 2-ethoxyethan-1-ol; 00056