Mixture of Ethanol + Diphenyl carbonate

Datasets

1. Mole fraction (2)
2. T_fus - Solid-liquid equilibrium temperature, K (2)

Mole fraction of Diphenyl carbonate (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Temperature, K - Liquid	Mole fraction of Diphenyl carbonate (2) - Liquid
283.00	0.0073
288.00	0.0087
293.00	0.0106
298.00	0.0134
303.00	0.0186
308.00	0.0257
313.00	0.0414
318.00	0.0701
323.00	0.1205
328.00	0.2349

Mole fraction of Diphenyl carbonate (2) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Temperature, K - Liquid	Mole fraction of Diphenyl carbonate (2) - Liquid
283.00	0.0073
288.00	0.0087
293.00	0.0106
298.00	0.0134
303.00	0.0186
308.00	0.0257
313.00	0.0414
318.00	0.0701
323.00	0.1205
328.00	0.2349

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0000	352.70
0.1020	348.06
0.2084	344.64
0.3002	341.27
0.4054	337.44
0.5012	335.80
0.5988	333.97
0.6998	331.57
0.8006	329.76
0.8498	328.12
0.8746	326.50
0.9005	324.47
0.9096	323.72
0.9205	322.22
0.9299	320.56
0.9399	319.11
0.9499	316.13
0.9603	312.43
0.9702	307.25
0.9802	300.31
0.9901	286.50

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Ethanol (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0000	352.70
0.1020	348.06
0.2084	344.64
0.3002	341.27
0.4054	337.44
0.5012	335.80
0.5988	333.97
0.6998	331.57
0.8006	329.76
0.8498	328.12
0.8746	326.50
0.9005	324.47
0.9096	323.72
0.9205	322.22
0.9299	320.56
0.9399	319.11
0.9499	316.13
0.9603	312.43
0.9702	307.25
0.9802	300.31
0.9901	286.50

Sources

• Solid-liquid equilibria for selected binary systems containing diphenyl carbonate
• Solubility of Diphenyl Carbonate in Pure Alcohols from (283 to 333) K