Mixture of Carbonic acid, dimethyl ester + Anisole

Datasets

1. Eutectic temperature, K (2)
2. n₀ - Refractive index (Na D-line) (4)
3. ρ_l - Mass density, kg/m3 (4)
4. T_fus - Solid-liquid equilibrium temperature, K (4)

Eutectic temperature, K [ref]

Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Eutectic temperature, K - Liquid
0.2364	228.86

Eutectic temperature, K [ref]

Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Eutectic temperature, K - Liquid
0.2364	228.86

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Anisole (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0502	1.3759
0.0997	1.3847
0.1995	1.402
0.2996	1.4178
0.3999	1.4334
0.4998	1.4485
0.5999	1.4629
0.6999	1.4766
0.8000	1.4898
0.9003	1.5027
0.9503	1.5087

Refractive index (Na D-line) [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 323.15 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.5012
0.0500	1.4963
0.1001	1.4908
0.2001	1.4795
0.3000	1.4659
0.4000	1.4516
0.5000	1.437
0.5999	1.4226
0.7000	1.4087
0.8000	1.393
0.9000	1.3754
0.9500	1.3655
1.0000	1.3546

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Anisole (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0502	1.3759
0.0997	1.3847
0.1995	1.402
0.2996	1.4178
0.3999	1.4334
0.4998	1.4485
0.5999	1.4629
0.6999	1.4766
0.8000	1.4898
0.9003	1.5027
0.9503	1.5087

Refractive index (Na D-line) [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 323.15 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.5012
0.0500	1.4963
0.1001	1.4908
0.2001	1.4795
0.3000	1.4659
0.4000	1.4516
0.5000	1.437
0.5999	1.4226
0.7000	1.4087
0.8000	1.393
0.9000	1.3754
0.9500	1.3655
1.0000	1.3546

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Anisole (2) - Liquid	Mass density, kg/m3 - Liquid
0.0502	1058.1
0.0997	1053.35
0.1995	1044.2
0.2996	1035.64
0.3999	1027.62
0.4998	1020.13
0.5999	1013.15
0.6999	1006.64
0.8000	1000.51
0.9003	994.65
0.9503	991.82

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 323.15 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	965.35
0.0500	967.83
0.1001	970.34
0.2001	975.5
0.3000	980.89
0.4000	986.63
0.5000	992.69
0.5999	999.08
0.7000	1005.87
0.8000	1013.1
0.9000	1020.95
0.9500	1025.2
1.0000	1029.81

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Anisole (2) - Liquid	Mass density, kg/m3 - Liquid
0.0502	1058.1
0.0997	1053.35
0.1995	1044.2
0.2996	1035.64
0.3999	1027.62
0.4998	1020.13
0.5999	1013.15
0.6999	1006.64
0.8000	1000.51
0.9003	994.65
0.9503	991.82

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 323.15 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	965.35
0.0500	967.83
0.1001	970.34
0.2001	975.5
0.3000	980.89
0.4000	986.63
0.5000	992.69
0.5999	999.08
0.7000	1005.87
0.8000	1013.1
0.9000	1020.95
0.9500	1025.2
1.0000	1029.81

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0000	235.20
0.0533	233.60
0.0864	233.00
0.1800	230.00
0.2000	229.10
0.2200	228.70

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.2499	230.10
0.2800	232.60
0.3002	235.20
0.4002	242.00
0.5012	249.70
0.6091	256.30
0.6970	261.70
0.8000	267.40
0.9002	272.60
0.9501	275.10
1.0000	278.20

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0000	235.20
0.0533	233.60
0.0864	233.00
0.1800	230.00
0.2000	229.10
0.2200	228.70

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.2499	230.10
0.2800	232.60
0.3002	235.20
0.4002	242.00
0.5012	249.70
0.6091	256.30
0.6970	261.70
0.8000	267.40
0.9002	272.60
0.9501	275.10
1.0000	278.20

Sources

• Ternary liquid-liquid equilibria and binary excess and deviation properties at constant temperature for mixtures of dimethyl carbonate, anisole, methanol, phenol and water
• The solid-liquid equilitbrium, excess molar volume and refractive deviation properties of binary systems containing dimethyl carbonate, anisole and phenol