Isobaric vapor-liquid phase equilibria for the binary systems of tert-butanol + 2-ethyl-1-hexanol and n-butanol + 2-ethyl-1-hexanol Ghanadzadeh, H.; Ghanadzadeh, A.; Sariri, R.; Boshra, A.; Fluid Phase Equilibria 2005, 233, 123-128
Data
P = 101.3 kPa
x (mol mol-1) x (mol mol-1)
0 0.0008
0.6500 0.9235
0.8600 0.9567
0.9270 0.9768
0.0112 0.3245
0.0200 0.398
0.0900 0.7289
0.1685 0.8125
0.3000 0.8703
0.3400 0.8845
0.4400 0.911
0.5100 0.9234
29971; butan-1-ol + 2-ethyl-1-hexanol; 00081:00435