Mixture of Phenol, 2-methyl- + Water

Datasets

1. Mole fraction (12)
2. ρ_l - Mass density, kg/m3 (2)

Mole fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1
298.15	0.0042
303.15	0.0044
308.15	0.0046
313.15	0.0047
318.15	0.0048
323.15	0.0051

Mole fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 2
298.15	0.5152
303.15	0.5102
308.15	0.5046
313.15	0.4990
318.15	0.4944
323.15	0.4846

Mass fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Temperature, K - Liquid mixture 1	Mass fraction of Phenol, 2-methyl- (1) - Liquid mixture 2
323.15	0.8498
298.15	0.8619

Mass fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Temperature, K - Liquid mixture 1	Mass fraction of Phenol, 2-methyl- (1) - Liquid mixture 1
323.15	0.0320
298.15	0.0284

Mole fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Temperature, K - Liquid mixture 1	Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 2
333.20	0.4866
343.20	0.4614

Mole fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Temperature, K - Liquid mixture 1	Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1
333.20	0.0053
343.20	0.0059

Mole fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1
298.15	0.0042
303.15	0.0044
308.15	0.0046
313.15	0.0047
318.15	0.0048
323.15	0.0051

Mole fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 2
298.15	0.5152
303.15	0.5102
308.15	0.5046
313.15	0.4990
318.15	0.4944
323.15	0.4846

Mass fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Temperature, K - Liquid mixture 1	Mass fraction of Phenol, 2-methyl- (1) - Liquid mixture 2
323.15	0.8498
298.15	0.8619

Mass fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Temperature, K - Liquid mixture 1	Mass fraction of Phenol, 2-methyl- (1) - Liquid mixture 1
323.15	0.0320
298.15	0.0284

Mole fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Temperature, K - Liquid mixture 1	Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 2
333.20	0.4866
343.20	0.4614

Mole fraction of Phenol, 2-methyl- (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)

Temperature, K - Liquid mixture 1	Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1
333.20	0.0053
343.20	0.0059

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Phenol, 2-methyl- (1) - Liquid	Mass density, kg/m3 - Liquid
0.5953	1033.22
0.6750	1034.33
0.8012	1035.55
0.8184	1035.9
0.8443	1036.16
0.8903	1036.47
0.8909	1036.26
0.9409	1036.95

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Phenol, 2-methyl- (1) - Liquid	Mass density, kg/m3 - Liquid
0.5953	1033.22
0.6750	1034.33
0.8012	1035.55
0.8184	1035.9
0.8443	1036.16
0.8903	1036.47
0.8909	1036.26
0.9409	1036.95

Sources

• Phase equilibria of phenolic compounds in water or ethanol
• Measurement and thermodynamic modeling of ternary (liquid + liquid) equilibrium for extraction of o-cresol, m-cresol or p-cresol from aqueous solution with 2-pentanone
• Extraction of o-, m- and p-cresol from aqueous solution with methyl isopropyl ketone: Equilibrium, correlations, and COSMO-RS predictions
• Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water