Mixture of Toluene + 1,2-Ethanediol

Datasets

1. Activity coefficient (2)
2. Mole fraction (32)

Activity coefficient of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Temperature, K - Liquid	Activity coefficient of Toluene (1) - Liquid
323.15	55.15
343.15	46.71
363.15	39.65
383.15	33.26

Activity coefficient of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Temperature, K - Liquid	Activity coefficient of Toluene (1) - Liquid
323.15	55.15
343.15	46.71
363.15	39.65
383.15	33.26

Mole fraction of Toluene (1) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 1
283.15	0.0195
293.15	0.0203
303.15	0.0217
313.15	0.0228
323.15	0.0246
333.15	0.0263

Mole fraction of Toluene (1) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 2
283.15	0.9974
293.15	0.9967
303.15	0.9951
313.15	0.9944
323.15	0.9933
333.15	0.9914

Mole fraction of Toluene (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 1
323.15	101.00	0.0242

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of Toluene (1) - Liquid mixture 2
303.15	0.9980
323.15	0.9959

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 1
307.86	0.9964
320.94	0.9915
333.64	0.9907
344.14	0.9884
351.60	0.9876
356.65	0.9827
363.86	0.9826
373.34	0.9807
383.13	0.9735
389.27	0.9699
398.54	0.9574
404.64	0.9504
411.65	0.9354

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 2
307.86	0.0258
320.94	0.0289
333.64	0.0305
344.14	0.0372
351.60	0.0357
356.65	0.0372
363.86	0.0415
373.34	0.0340
383.13	0.0380
389.27	0.0414
398.54	0.0461
404.64	0.0499
411.65	0.0660

Mole fraction of Toluene (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of Toluene (1) - Liquid mixture 1
323.15	101.30	0.9922

Mole fraction of Toluene (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of Toluene (1) - Liquid mixture 2
323.15	101.30	0.0281

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

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

Temperature, K - Liquid mixture 1	Mass fraction of 1,2-Ethanediol (2) - Liquid mixture 2
303.15	0.9684
323.15	0.9654
313.15	0.9673

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

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

Temperature, K - Liquid mixture 1	Mass fraction of 1,2-Ethanediol (2) - Liquid mixture 1
303.15	0.0022
323.15	0.0037
313.15	0.0027

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

Fixed		Measured
Pressure, kPa - Liquid mixture 1	Temperature, K - Liquid mixture 1	Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 1
101.30	303.15	0.0023

Mole fraction of Toluene (1) [ref]

Fixed		Measured
Pressure, kPa - Liquid mixture 2	Temperature, K - Liquid mixture 2	Mole fraction of Toluene (1) - Liquid mixture 2
101.30	303.15	0.0213

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 1
293.15	0.9989
303.15	0.9983
313.15	0.9975
323.15	0.9965
333.15	0.9950
343.15	0.9922
353.15	0.9888
363.15	0.9850

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 2
293.15	0.0199
303.15	0.0189
313.15	0.0273
323.15	0.0256
333.15	0.0272
343.15	0.0292
353.15	0.0282
363.15	0.0343

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

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

Temperature, K - Liquid mixture 2	Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 2
279.10	0.0010
297.90	0.0021
302.10	0.0025
312.10	0.0032
316.30	0.0038
323.20	0.0047
331.20	0.0060
345.10	0.0096
357.10	0.0147
361.00	0.0167

Mole fraction of Toluene (1) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 1
279.10	0.0188
297.90	0.0201
302.10	0.0209
312.10	0.0219
316.30	0.0226
323.20	0.0238
331.20	0.0255
345.10	0.0281
357.10	0.0305
361.00	0.0317

Mole fraction of Toluene (1) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 1
283.15	0.0195
293.15	0.0203
303.15	0.0217
313.15	0.0228
323.15	0.0246
333.15	0.0263

Mole fraction of Toluene (1) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 2
283.15	0.9974
293.15	0.9967
303.15	0.9951
313.15	0.9944
323.15	0.9933
333.15	0.9914

Mole fraction of Toluene (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 1
323.15	101.00	0.0242

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 2)

Temperature, K - Liquid mixture 2	Mole fraction of Toluene (1) - Liquid mixture 2
303.15	0.9980
323.15	0.9959

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 1
307.86	0.9964
320.94	0.9915
333.64	0.9907
344.14	0.9884
351.60	0.9876
356.65	0.9827
363.86	0.9826
373.34	0.9807
383.13	0.9735
389.27	0.9699
398.54	0.9574
404.64	0.9504
411.65	0.9354

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 2
307.86	0.0258
320.94	0.0289
333.64	0.0305
344.14	0.0372
351.60	0.0357
356.65	0.0372
363.86	0.0415
373.34	0.0340
383.13	0.0380
389.27	0.0414
398.54	0.0461
404.64	0.0499
411.65	0.0660

Mole fraction of Toluene (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of Toluene (1) - Liquid mixture 1
323.15	101.30	0.9922

Mole fraction of Toluene (1) [ref]

Fixed		Measured
Temperature, K - Liquid mixture 2	Pressure, kPa - Liquid mixture 2	Mole fraction of Toluene (1) - Liquid mixture 2
323.15	101.30	0.0281

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

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

Temperature, K - Liquid mixture 1	Mass fraction of 1,2-Ethanediol (2) - Liquid mixture 2
303.15	0.9684
323.15	0.9654
313.15	0.9673

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

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

Temperature, K - Liquid mixture 1	Mass fraction of 1,2-Ethanediol (2) - Liquid mixture 1
303.15	0.0022
323.15	0.0037
313.15	0.0027

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

Fixed		Measured
Pressure, kPa - Liquid mixture 1	Temperature, K - Liquid mixture 1	Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 1
101.30	303.15	0.0023

Mole fraction of Toluene (1) [ref]

Fixed		Measured
Pressure, kPa - Liquid mixture 2	Temperature, K - Liquid mixture 2	Mole fraction of Toluene (1) - Liquid mixture 2
101.30	303.15	0.0213

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 1
293.15	0.9989
303.15	0.9983
313.15	0.9975
323.15	0.9965
333.15	0.9950
343.15	0.9922
353.15	0.9888
363.15	0.9850

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 2
293.15	0.0199
303.15	0.0189
313.15	0.0273
323.15	0.0256
333.15	0.0272
343.15	0.0292
353.15	0.0282
363.15	0.0343

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

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

Temperature, K - Liquid mixture 2	Mole fraction of 1,2-Ethanediol (2) - Liquid mixture 2
279.10	0.0010
297.90	0.0021
302.10	0.0025
312.10	0.0032
316.30	0.0038
323.20	0.0047
331.20	0.0060
345.10	0.0096
357.10	0.0147
361.00	0.0167

Mole fraction of Toluene (1) [ref]

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

Temperature, K - Liquid mixture 1	Mole fraction of Toluene (1) - Liquid mixture 1
279.10	0.0188
297.90	0.0201
302.10	0.0209
312.10	0.0219
316.30	0.0226
323.20	0.0238
331.20	0.0255
345.10	0.0281
357.10	0.0305
361.00	0.0317

Sources

• Binary liquid liquid equilibrium in the systems containing monofunctional benzene derivates and 1,2-ethanediol
• Liquid-liquid equilibrium data for binary systems containing o-dichlorobenzene and nitrobenzene
• Liquid-liquid equilibria for toluene/heptane + phenol/cresols + ethylene glycol system
• Solvent screening and liquid-liquid measurement for extraction of phenols from aromatic hydrocarbon mixtures
• Liquid Liquid Equilibria of Binary, Ternary, and Quaternary Systems Involving Monoethylene Glycol, Water, Toluene, p-Xylene, Hexane, and Octane
• Experimental Determination and Modeling of Liquid-Liquid Equilibrium for Ternary Mixtures of Ethylene Glycol + 1,2-Butanediol + 3-Heptanone or Anisole
• Infinite Dilution Activity Coefficients in Ethylene Glycol and Ethylene Carbonate
• Liquid-Liquid Equilibria for Binary and Ternary Systems Containing Glycols, Aromatic Hydrocarbons, and Water: Experimental Measurements and Modeling with the CPA EoS