Mixture of Acetic acid, 2-methylpropyl ester + 1-Hexanol

Datasets

1. Mole fraction
2. T_boil - Boiling temperature at pressure P, K

Mole fraction of Acetic acid, 2-methylpropyl ester (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid, 2-methylpropyl ester (1) - Liquid	Mole fraction of Acetic acid, 2-methylpropyl ester (1) - Gas
0.0000	0.0000
0.0410	0.1290
0.0780	0.2410
0.1350	0.3660
0.1910	0.4840
0.2650	0.5840
0.3210	0.6550
0.3720	0.6980
0.4270	0.7400
0.4750	0.7840
0.5360	0.8180
0.5960	0.8440
0.6570	0.8810
0.6990	0.8950
0.7530	0.9170
0.8060	0.9370
0.8530	0.9550
0.9000	0.9690
0.9400	0.9820
0.9740	0.9920
1.0000	1.0000

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetic acid, 2-methylpropyl ester (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	430.06
0.0410	427.08
0.0780	424.37
0.1350	420.74
0.1910	417.06
0.2650	413.15
0.3210	410.38
0.3720	408.49
0.4270	406.08
0.4750	404.05
0.5360	402.10
0.5960	400.38
0.6570	398.44
0.6990	397.06
0.7530	395.71
0.8060	394.29
0.8530	393.17
0.9000	392.06
0.9400	391.09
0.9740	390.35
1.0000	389.90

Sources

• 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