Mixture of Ethylbenzene + Phenol + Water

Datasets

1. Mole fraction (2)

Mole fraction of Phenol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Ethylbenzene (1) - Liquid mixture 1	Mole fraction of Phenol (2) - Liquid mixture 1
298.15	0.0000	0.3123
298.15	0.1331	0.4343
298.15	0.1625	0.4249
298.15	0.2312	0.4333
298.15	0.3106	0.4078
298.15	0.3321	0.4002
298.15	0.3508	0.3912
298.15	0.4985	0.3291
298.15	0.5822	0.2823
298.15	0.5930	0.2789
298.15	0.6696	0.2240
298.15	0.6886	0.2251
298.15	0.9239	0.0226
323.15	0.0000	0.2420
323.15	0.0411	0.3553
323.15	0.0525	0.3670
323.15	0.0592	0.3721
323.15	0.1189	0.4121
323.15	0.1463	0.4150
323.15	0.1613	0.4179
323.15	0.1624	0.4144
323.15	0.1850	0.4145
323.15	0.2131	0.4125
323.15	0.2491	0.4100
323.15	0.2882	0.4040
323.15	0.2892	0.4040
323.15	0.3644	0.3790
323.15	0.5030	0.3186
323.15	0.7504	0.1736

Mole fraction of Phenol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Ethylbenzene (1) - Liquid mixture 1	Mole fraction of Phenol (2) - Liquid mixture 1
298.15	0.0000	0.3123
298.15	0.1331	0.4343
298.15	0.1625	0.4249
298.15	0.2312	0.4333
298.15	0.3106	0.4078
298.15	0.3321	0.4002
298.15	0.3508	0.3912
298.15	0.4985	0.3291
298.15	0.5822	0.2823
298.15	0.5930	0.2789
298.15	0.6696	0.2240
298.15	0.6886	0.2251
298.15	0.9239	0.0226
323.15	0.0000	0.2420
323.15	0.0411	0.3553
323.15	0.0525	0.3670
323.15	0.0592	0.3721
323.15	0.1189	0.4121
323.15	0.1463	0.4150
323.15	0.1613	0.4179
323.15	0.1624	0.4144
323.15	0.1850	0.4145
323.15	0.2131	0.4125
323.15	0.2491	0.4100
323.15	0.2882	0.4040
323.15	0.2892	0.4040
323.15	0.3644	0.3790
323.15	0.5030	0.3186
323.15	0.7504	0.1736

Sources

• Liquid-Liquid Equilibria in Ternary Systems of Aromatic Hydrocarbons (Toluene or Ethylbenzene) + Phenols + Water