Mixture of 2-Naphthalenecarboxaldehyde + Ethyl Acetate

Datasets

1. Mole fraction (2)
2. ρ_l - Mass density, kg/m3 (2)
3. T_fus - Solid-liquid equilibrium temperature, K (2)

Mole fraction of 2-Naphthalenecarboxaldehyde (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Temperature, K - Liquid	Mole fraction of 2-Naphthalenecarboxaldehyde (1) - Liquid
283.15	0.1480
288.15	0.1837
293.15	0.2212
298.15	0.2681
303.15	0.3316
308.15	0.4266
313.15	0.5347

Mole fraction of 2-Naphthalenecarboxaldehyde (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Temperature, K - Liquid	Mole fraction of 2-Naphthalenecarboxaldehyde (1) - Liquid
283.15	0.1480
288.15	0.1837
293.15	0.2212
298.15	0.2681
303.15	0.3316
308.15	0.4266
313.15	0.5347

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of 2-Naphthalenecarboxaldehyde (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.2851	944.0
298.15	0.3937	957.0
308.15	0.5686	975.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mass fraction of 2-Naphthalenecarboxaldehyde (1) - Liquid	Mass density, kg/m3 - Liquid
288.15	0.2851	944.0
298.15	0.3937	957.0
308.15	0.5686	975.0

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mass fraction of 2-Naphthalenecarboxaldehyde (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.2851	288.15
0.3937	298.15
0.5686	308.15

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mass fraction of 2-Naphthalenecarboxaldehyde (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.2851	288.15
0.3937	298.15
0.5686	308.15

Sources

• Solid-Liquid Phase Equilibria of the Ternary System (2-Naphthaldehyde + 4-Methylphthalic Anhydride + Ethyl Acetate) at (288.15, 298.15, and 308.15) K