Mixture of Diethyl carbonate + Diphenyl carbonate

Datasets

1. P_vap - Vapor or sublimation pressure, kPa
2. T_fus - Solid-liquid equilibrium temperature, K

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Diethyl carbonate (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
373.20	0.1280	5.40
373.20	0.2200	10.10
373.20	0.3370	15.90
373.20	0.4750	21.40
373.20	0.6090	26.70
373.20	0.7160	31.90
373.20	0.8190	37.30
373.20	0.9160	40.50
413.20	0.1280	20.40
413.20	0.2200	34.70
413.20	0.3370	53.70
413.20	0.4280	67.70
413.20	0.5240	82.60
413.20	0.6090	92.50
413.20	0.7160	107.00
413.20	0.8180	121.60
413.20	0.9160	135.60
453.20	0.1280	43.40
453.20	0.2200	75.70
453.20	0.3370	127.50
453.20	0.4280	160.70
453.20	0.5110	191.10
453.20	0.6090	220.50
453.20	0.7160	261.60
453.20	0.8190	295.70
453.20	0.9040	336.90

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Diethyl carbonate (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0000	352.70
0.1168	346.65
0.2008	342.90
0.3022	337.18
0.4026	331.13
0.5034	324.31
0.6045	316.30
0.7028	306.22
0.7989	292.53
0.8994	269.46
0.9507	247.28

Sources

• Solid-liquid equilibria for selected binary systems containing diphenyl carbonate
• Isothermal (vapour + liquid) equilibrium (VLE) for binary mixtures containing diethyl carbonate, phenyl acetate, diphenyl carbonate, or ethyl acetate

Note: These property values are available through the Cheméo API. A free account gives you an access key.