Mixture of Carbonic acid, dimethyl ester + Propanoic acid, 2-hydroxy-, ethyl ester + Methyl Alcohol

Datasets

1. T_boil - Boiling temperature at pressure P, K (2)

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Mole fraction of Methyl Alcohol (3) - Liquid	Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	0.9500	364.91
0.0949	0.8551	354.90
0.1901	0.7599	348.73
0.2849	0.6651	344.63
0.3800	0.5700	342.40
0.4751	0.4749	340.17
0.5701	0.3799	339.62
0.6650	0.2850	338.64
0.7603	0.1897	338.22
0.8550	0.0950	338.44
0.9500	0.0000	339.52
0.0000	0.8800	366.97
0.0881	0.7919	358.56
0.1760	0.7040	352.58
0.2638	0.6162	348.34
0.3522	0.5278	344.83
0.4401	0.4399	342.90
0.5280	0.3520	342.02
0.6161	0.2639	340.99
0.7042	0.1758	340.20
0.7921	0.0879	340.25
0.8800	0.0000	342.02

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Mole fraction of Methyl Alcohol (3) - Liquid	Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	0.9500	364.91
0.0949	0.8551	354.90
0.1901	0.7599	348.73
0.2849	0.6651	344.63
0.3800	0.5700	342.40
0.4751	0.4749	340.17
0.5701	0.3799	339.62
0.6650	0.2850	338.64
0.7603	0.1897	338.22
0.8550	0.0950	338.44
0.9500	0.0000	339.52
0.0000	0.8800	366.97
0.0881	0.7919	358.56
0.1760	0.7040	352.58
0.2638	0.6162	348.34
0.3522	0.5278	344.83
0.4401	0.4399	342.90
0.5280	0.3520	342.02
0.6161	0.2639	340.99
0.7042	0.1758	340.20
0.7921	0.0879	340.25
0.8800	0.0000	342.02

Sources

• Separation Effects of Renewable Solvent Ethyl Lactate on the Vapor Liquid Equilibria of the Methanol + Dimethyl Carbonate Azeotropic System