Mixture of Eicosane + Di-n-propyl ether

Datasets

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

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Eicosane (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.9540	309.55
0.9740	310.00
1.0000	310.30

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Eicosane (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0263	275.05
0.0315	276.45
0.0377	278.05
0.0459	279.85
0.0559	281.65
0.0703	283.75
0.0873	285.55
0.1084	287.55
0.1310	289.15
0.1598	290.95
0.1898	292.55
0.2245	294.05
0.2635	295.65
0.3090	297.20
0.3500	298.45
0.3900	299.65
0.4380	300.80
0.4910	301.95
0.5340	302.85
0.5750	303.65
0.6180	304.45
0.6600	305.15
0.7080	305.95
0.7440	306.55
0.7870	307.20
0.8310	307.85
0.8740	308.50
0.9030	308.75
0.9260	309.10

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Eicosane (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.9540	309.55
0.9740	310.00
1.0000	310.30

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Eicosane (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0263	275.05
0.0315	276.45
0.0377	278.05
0.0459	279.85
0.0559	281.65
0.0703	283.75
0.0873	285.55
0.1084	287.55
0.1310	289.15
0.1598	290.95
0.1898	292.55
0.2245	294.05
0.2635	295.65
0.3090	297.20
0.3500	298.45
0.3900	299.65
0.4380	300.80
0.4910	301.95
0.5340	302.85
0.5750	303.65
0.6180	304.45
0.6600	305.15
0.7080	305.95
0.7440	306.55
0.7870	307.20
0.8310	307.85
0.8740	308.50
0.9030	308.75
0.9260	309.10

Sources

• Solubilities of Some Long-Chain n-Alkanes in Dipropyl Ether, Dibutyl Ether, 1-Chlorobutane, and 1-Chlorooctane as Functions of Temperature