Mixture of Isopropyl Alcohol + 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	0.0051
288.00	0.0071
293.00	0.0087
298.00	0.0105
303.00	0.0156
308.00	0.0204
313.00	0.0331
318.00	0.0511
323.00	0.0828
328.00	0.1396

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	0.0051
288.00	0.0071
293.00	0.0087
298.00	0.0105
303.00	0.0156
308.00	0.0204
313.00	0.0331
318.00	0.0511
323.00	0.0828
328.00	0.1396

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Isopropyl Alcohol (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0000	352.70
0.1005	349.23
0.1991	346.10
0.3149	342.27
0.4001	340.32
0.5003	337.61
0.5994	335.54
0.7014	333.32
0.7997	330.98
0.8496	329.06
0.9002	326.09
0.9125	325.97
0.9202	324.32
0.9294	322.87
0.9399	321.06
0.9499	318.89
0.9600	315.91
0.9700	312.20
0.9800	306.26
0.9900	294.35

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Isopropyl Alcohol (1) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.0000	352.70
0.1005	349.23
0.1991	346.10
0.3149	342.27
0.4001	340.32
0.5003	337.61
0.5994	335.54
0.7014	333.32
0.7997	330.98
0.8496	329.06
0.9002	326.09
0.9125	325.97
0.9202	324.32
0.9294	322.87
0.9399	321.06
0.9499	318.89
0.9600	315.91
0.9700	312.20
0.9800	306.26
0.9900	294.35

Sources

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