Mixture of Butanenitrile + 1-Decanol

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-Decanol (2) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0172	253.42
0.0240	256.66
0.0354	260.02
0.0523	263.37
0.0669	265.36
0.0820	266.77
0.1012	267.98
0.1328	269.39
0.1710	270.59
0.2088	271.34
0.2540	271.98
0.2967	272.43
0.3325	272.63
0.3895	273.16
0.4261	273.34
0.4672	273.57
0.5222	273.84
0.5607	274.05
0.6004	274.44
0.6513	275.19
0.7116	276.02
0.7518	276.36
0.7952	276.72
0.8447	277.19
0.8955	277.69
0.9395	278.30
0.9640	278.50
1.0000	278.67

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Decanol (2) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0172	253.42
0.0240	256.66
0.0354	260.02
0.0523	263.37
0.0669	265.36
0.0820	266.77
0.1012	267.98
0.1328	269.39
0.1710	270.59
0.2088	271.34
0.2540	271.98
0.2967	272.43
0.3325	272.63
0.3895	273.16
0.4261	273.34
0.4672	273.57
0.5222	273.84
0.5607	274.05
0.6004	274.44
0.6513	275.19
0.7116	276.02
0.7518	276.36
0.7952	276.72
0.8447	277.19
0.8955	277.69
0.9395	278.30
0.9640	278.50
1.0000	278.67

Sources

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