Mixture of Phenol + Water

Datasets

1. Mole fraction (20)
2. ρ_l - Mass density, kg/m3 (2)
3. Binary diffusion coefficient, m2/s (2)

Mole fraction of Water (2) [ref]

Fixed		Measured
Pressure, kPa - Liquid mixture 2	Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
101.00	328.15	0.6700

Mole fraction of Water (2) [ref]

Fixed		Measured
Pressure, kPa - Liquid mixture 2	Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 2
101.00	328.15	0.1255

Mole fraction of Phenol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of Phenol (1) - Liquid mixture 2
298.15	101.00	0.3280

Mole fraction of Phenol (1) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid mixture 2)
• Pressure, kPa = 101 (Liquid mixture 2)

Mole fraction of Phenol (1) - Liquid mixture 1
0.0160
0.0170

Mole fraction of Phenol (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Phenol (1) - Liquid
298.15	101.00	0.8030

Mole fraction of Phenol (1) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of Phenol (1) - Liquid mixture 1
298.15	0.0172
303.15	0.0184
308.15	0.0195
313.15	0.0207
318.15	0.0217
323.15	0.0242

Mass fraction of Phenol (1) [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid mixture 1)
• Pressure, kPa = 101 (Liquid mixture 1)

Mass fraction of Phenol (1) - Liquid mixture 1
0.7059
0.0827

Mole fraction of Phenol (1) [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Phenol (1) - Liquid mixture 1
283.15	0.0156
298.15	0.0174
313.15	0.0214

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 2
283.15	0.6301
298.15	0.6731
313.15	0.7244

Mole fraction of Water (2) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
298.15	0.6877
313.15	0.7245
318.15	0.7400
323.15	0.7580
328.15	0.7835
333.15	0.8068

Mole fraction of Water (2) [ref]

Fixed		Measured
Pressure, kPa - Liquid mixture 2	Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
101.00	328.15	0.6700

Mole fraction of Water (2) [ref]

Fixed		Measured
Pressure, kPa - Liquid mixture 2	Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 2
101.00	328.15	0.1255

Mole fraction of Phenol (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of Phenol (1) - Liquid mixture 2
298.15	101.00	0.3280

Mole fraction of Phenol (1) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid mixture 2)
• Pressure, kPa = 101 (Liquid mixture 2)

Mole fraction of Phenol (1) - Liquid mixture 1
0.0160
0.0170

Mole fraction of Phenol (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Phenol (1) - Liquid
298.15	101.00	0.8030

Mole fraction of Phenol (1) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of Phenol (1) - Liquid mixture 1
298.15	0.0172
303.15	0.0184
308.15	0.0195
313.15	0.0207
318.15	0.0217
323.15	0.0242

Mass fraction of Phenol (1) [ref]

Operational conditions:

• Temperature, K = 298.2 (Liquid mixture 1)
• Pressure, kPa = 101 (Liquid mixture 1)

Mass fraction of Phenol (1) - Liquid mixture 1
0.7059
0.0827

Mole fraction of Phenol (1) [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Phenol (1) - Liquid mixture 1
283.15	0.0156
298.15	0.0174
313.15	0.0214

Mole fraction of Water (2) [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 2
283.15	0.6301
298.15	0.6731
313.15	0.7244

Mole fraction of Water (2) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of Water (2) - Liquid mixture 1
298.15	0.6877
313.15	0.7245
318.15	0.7400
323.15	0.7580
328.15	0.7835
333.15	0.8068

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 313.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Phenol (1) - Liquid	Mass density, kg/m3 - Liquid
0.3794	1038.84
0.4653	1042.74
0.6176	1048.12
0.7052	1050.69
0.8247	1054.06
0.9099	1056.28

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 313.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Phenol (1) - Liquid	Mass density, kg/m3 - Liquid
0.3794	1038.84
0.4653	1042.74
0.6176	1048.12
0.7052	1050.69
0.8247	1054.06
0.9099	1056.28

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Binary diffusion coefficient, m2/s - Liquid
298.20	0.0000
303.20	0.0000
313.20	0.0000
323.20	0.0000
333.20	0.0000
343.20	0.0000
353.20	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Binary diffusion coefficient, m2/s - Liquid
298.20	0.0000
303.20	0.0000
313.20	0.0000
323.20	0.0000
333.20	0.0000
343.20	0.0000
353.20	0.0000

Sources

• Ternary liquid-liquid equilibria and binary excess and deviation properties at constant temperature for mixtures of dimethyl carbonate, anisole, methanol, phenol and water
• Extraction of phenolic compounds from aqueous solution using choline bis(trifluoromethylsulfonyl)imide
• Phase equilibria of phenolic compounds in water or ethanol
• Tie-line data for the aqueous solutions of phenol with organic solvents at T = 298.2 K
• (Liquid + liquid) extraction of phenols from aqueous solutions with cineole
• Liquid-Liquid Equilibria in Ternary Systems of Aromatic Hydrocarbons (Toluene or Ethylbenzene) + Phenols + Water
• Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water
• Infinite Dilution Binary Diffusion Coefficients for Compounds Derived from Biomass in Water at 0.1 MPa and Temperatures from (298.2 to 353.2) K