Mixture of 1-Undecanol + Butanenitrile

Datasets

1. T_fus - Solid-liquid equilibrium temperature, K (2)

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Undecanol (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0141	257.30
0.0246	265.44
0.0373	269.51
0.0501	271.77
0.0807	275.00
0.1094	276.73
0.1366	278.11
0.1814	279.42
0.2222	280.21
0.2668	281.07
0.3146	281.62
0.3570	281.96
0.4061	282.37
0.4761	282.86
0.5242	283.30
0.5846	283.53
0.6180	283.83
0.6534	284.42
0.6887	284.82
0.7188	285.15
0.7596	285.58
0.7930	285.97
0.8319	286.57
0.8640	287.15
0.8984	287.81
0.9335	288.39
0.9682	289.05
1.0000	289.63

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Undecanol (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0141	257.30
0.0246	265.44
0.0373	269.51
0.0501	271.77
0.0807	275.00
0.1094	276.73
0.1366	278.11
0.1814	279.42
0.2222	280.21
0.2668	281.07
0.3146	281.62
0.3570	281.96
0.4061	282.37
0.4761	282.86
0.5242	283.30
0.5846	283.53
0.6180	283.83
0.6534	284.42
0.6887	284.82
0.7188	285.15
0.7596	285.58
0.7930	285.97
0.8319	286.57
0.8640	287.15
0.8984	287.81
0.9335	288.39
0.9682	289.05
1.0000	289.63

Sources

• Experimental (Solid + Liquid) and (Liquid + Liquid) Equilibria and Excess Molar Volume of Alkanol + Acetonitrile, Propanenitrile, and Butanenitrile Mixtures