Mixture of 1-Decanol + 2-Tridecanone

Datasets

1. T_fus - Solid-liquid equilibrium temperature, K (4)

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of 2-Tridecanone (2) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0000	279.50
0.0220	279.30
0.0408	279.10
0.0648	279.20
0.0661	278.90

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of 2-Tridecanone (2) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.1061	279.20
0.1564	281.40
0.2051	284.30
0.2614	286.50
0.2953	287.50
0.3200	288.70
0.3416	290.40
0.3914	291.40
0.4297	291.90
0.4771	293.00
0.5217	293.80
0.5723	294.40
0.6092	295.30
0.6587	295.80
0.7084	296.50
0.7583	297.30
0.8057	297.80
0.8560	298.60
0.8976	299.60
0.9398	300.50
1.0000	300.80

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of 2-Tridecanone (2) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0000	279.50
0.0220	279.30
0.0408	279.10
0.0648	279.20
0.0661	278.90

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of 2-Tridecanone (2) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.1061	279.20
0.1564	281.40
0.2051	284.30
0.2614	286.50
0.2953	287.50
0.3200	288.70
0.3416	290.40
0.3914	291.40
0.4297	291.90
0.4771	293.00
0.5217	293.80
0.5723	294.40
0.6092	295.30
0.6587	295.80
0.7084	296.50
0.7583	297.30
0.8057	297.80
0.8560	298.60
0.8976	299.60
0.9398	300.50
1.0000	300.80

Sources

• Measurements, Correlations, and Mod. UNIFAC (Do) Prediction of (Solid-Liquid) Phase Equilibria Diagrams in Binary Systems (Aliphatic Ketone + an Alcohol)