Phase equilibria in the ternary system isobutyl alcohol + isobutyl acetate + 1-hexanol and the binary systems isobutyl alcohol + 1-hexanol, isobutyl acetate + 1-hexanol at 101.3 kPa Muñoz, R.; Montón, J.; Burguet, M.; de la Torre, J.; Fluid Phase Equilibria 2005, 235, 64-71
Data
T (K) P (kPa)
356.39 5.0
394.34 28.5
398.14 33.1
401.57 37.8
404.56 42.3
407.43 47.1
410.27 52.2
412.75 57.0
414.93 61.5
417.18 66.4
417.28 66.7
364.42 7.5
419.52 71.9
421.96 78.0
424.54 84.8
426.31 89.8
428.20 95.3
429.97 100.8
430.00 101.5
430.06 101.3
430.26 101.7
368.04 8.9
372.23 10.9
376.68 13.4
379.61 15.3
384.92 19.3
384.93 19.3
390.31 24.2
72; 1-hexanol; 00045