Mixture of Cyclohexanol + Toluene + Water

Datasets

1. Mole fraction (10)

Mole fraction of Cyclohexanol (1) [ref]

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

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Toluene (2) - Liquid mixture 1	Mole fraction of Cyclohexanol (1) - Liquid mixture 1
298.15	0.0000	0.5610
298.15	0.1300	0.5400
298.15	0.2120	0.5120
298.15	0.2710	0.4860
298.15	0.3010	0.4720
298.15	0.3360	0.4530
298.15	0.3830	0.4280
298.15	0.4870	0.3720
298.15	0.5360	0.3430
298.15	0.5960	0.3030
298.15	0.6670	0.2550
298.15	0.7520	0.1930
298.15	0.8600	0.1110
323.15	0.0000	0.5340
323.15	0.0950	0.5260
323.15	0.1410	0.5160
323.15	0.2100	0.5010
323.15	0.2530	0.4790
323.15	0.2850	0.4640
323.15	0.3270	0.4420
323.15	0.3850	0.4130
323.15	0.4610	0.3700
323.15	0.5890	0.2980
323.15	0.6600	0.2490
323.15	0.7490	0.1910
323.15	0.8570	0.1120

Temperature, K x Pressure, kPa x Mole fraction [ref]

Fixed			Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Toluene (2) - Liquid mixture 1	Mole fraction of Cyclohexanol (1) - Liquid mixture 1	Mole fraction of Cyclohexanol (1) - Gas	Mole fraction of Toluene (2) - Gas
333.15	21.77	0.2970	0.5830	0.0390	0.4780
333.15	25.54	0.0810	0.5720	0.0390	0.2470
333.15	25.77	0.5370	0.4050	0.0240	0.5030
333.15	30.83	0.3020	0.4950	0.0230	0.3460
363.15	64.30	0.3400	0.5850	0.0620	0.4600
363.15	79.70	0.5520	0.3880	0.0400	0.4170
363.15	85.76	0.0860	0.5480	0.0450	0.1550
363.15	91.02	0.1940	0.5470	0.0430	0.2710
363.15	95.62	0.3510	0.4740	0.0350	0.3190

Temperature, K x Pressure, kPa x Mole fraction [ref]

Fixed			Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Toluene (2) - Liquid mixture 1	Mole fraction of Cyclohexanol (1) - Liquid mixture 1	Mole fraction of Cyclohexanol (1) - Gas	Mole fraction of Toluene (2) - Gas
333.15	29.88	0.1500	0.5120	0.0270	0.3030
333.15	27.07	0.0810	0.5330	0.0320	0.2120
333.15	32.88	0.2820	0.4560	0.0180	0.3480
333.15	35.53	0.5430	0.3280	0.0250	0.3950
333.15	35.85	0.6090	0.2980	0.0180	0.4140
333.15	35.87	0.6560	0.2600	0.0170	0.4250
358.15	86.30	0.2090	0.4650	0.0350	0.2910
358.15	93.09	0.4000	0.3960	0.0290	0.3450
358.15	96.17	0.5710	0.3020	0.0240	0.3760

Mole fraction of Cyclohexanol (1) [ref]

Fixed			Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Toluene (2) - Liquid mixture 1	Mole fraction of Cyclohexanol (1) - Liquid mixture 1
333.15	29.88	0.1500	0.5120
333.15	27.07	0.0810	0.5330
333.15	32.88	0.2820	0.4560
333.15	35.53	0.5430	0.3280
333.15	35.85	0.6090	0.2980
333.15	35.87	0.6560	0.2600
358.15	86.30	0.2090	0.4650
358.15	93.09	0.4000	0.3960
358.15	96.17	0.5710	0.3020

Temperature, K x Mass fraction [ref]

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

Fixed		Measured
Temperature, K - Liquid mixture 2	Mass fraction of Cyclohexanol (1) - Liquid mixture 1	Mass fraction of Toluene (2) - Liquid mixture 1	Mass fraction of Toluene (2) - Liquid mixture 2	Mass fraction of Cyclohexanol (1) - Liquid mixture 2
303.15	0.0190	0.9797	0.0018	0.0053
323.15	0.0286	0.9700	0.0043	0.0048
323.15	0.0472	0.9513	0.0047	0.0067
323.15	0.0638	0.9352	0.0044	0.0086
323.15	0.0807	0.9177	0.0046	0.0096
323.15	0.0975	0.9013	0.0046	0.0109
323.15	0.1141	0.8835	0.0050	0.0114
323.15	0.1667	0.8306	0.0064	0.0144
303.15	0.0358	0.9615	0.0014	0.0082
303.15	0.0488	0.9491	0.0015	0.0099
303.15	0.0586	0.9391	0.0017	0.0108
303.15	0.0762	0.9215	0.0017	0.0120
303.15	0.1227	0.8752	0.0019	0.0144
303.15	0.1356	0.8623	0.0020	0.0155
303.15	0.1528	0.8451	0.0023	0.0159
323.15	0.0134	0.9849	0.0039	0.0025

Mole fraction of Cyclohexanol (1) [ref]

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

Fixed		Measured
Temperature, K - Liquid mixture 1	Mole fraction of Toluene (2) - Liquid mixture 1	Mole fraction of Cyclohexanol (1) - Liquid mixture 1
298.15	0.0000	0.5610
298.15	0.1300	0.5400
298.15	0.2120	0.5120
298.15	0.2710	0.4860
298.15	0.3010	0.4720
298.15	0.3360	0.4530
298.15	0.3830	0.4280
298.15	0.4870	0.3720
298.15	0.5360	0.3430
298.15	0.5960	0.3030
298.15	0.6670	0.2550
298.15	0.7520	0.1930
298.15	0.8600	0.1110
323.15	0.0000	0.5340
323.15	0.0950	0.5260
323.15	0.1410	0.5160
323.15	0.2100	0.5010
323.15	0.2530	0.4790
323.15	0.2850	0.4640
323.15	0.3270	0.4420
323.15	0.3850	0.4130
323.15	0.4610	0.3700
323.15	0.5890	0.2980
323.15	0.6600	0.2490
323.15	0.7490	0.1910
323.15	0.8570	0.1120

Temperature, K x Pressure, kPa x Mole fraction [ref]

Fixed			Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Toluene (2) - Liquid mixture 1	Mole fraction of Cyclohexanol (1) - Liquid mixture 1	Mole fraction of Cyclohexanol (1) - Gas	Mole fraction of Toluene (2) - Gas
333.15	21.77	0.2970	0.5830	0.0390	0.4780
333.15	25.54	0.0810	0.5720	0.0390	0.2470
333.15	25.77	0.5370	0.4050	0.0240	0.5030
333.15	30.83	0.3020	0.4950	0.0230	0.3460
363.15	64.30	0.3400	0.5850	0.0620	0.4600
363.15	79.70	0.5520	0.3880	0.0400	0.4170
363.15	85.76	0.0860	0.5480	0.0450	0.1550
363.15	91.02	0.1940	0.5470	0.0430	0.2710
363.15	95.62	0.3510	0.4740	0.0350	0.3190

Temperature, K x Pressure, kPa x Mole fraction [ref]

Fixed			Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Toluene (2) - Liquid mixture 1	Mole fraction of Cyclohexanol (1) - Liquid mixture 1	Mole fraction of Cyclohexanol (1) - Gas	Mole fraction of Toluene (2) - Gas
333.15	29.88	0.1500	0.5120	0.0270	0.3030
333.15	27.07	0.0810	0.5330	0.0320	0.2120
333.15	32.88	0.2820	0.4560	0.0180	0.3480
333.15	35.53	0.5430	0.3280	0.0250	0.3950
333.15	35.85	0.6090	0.2980	0.0180	0.4140
333.15	35.87	0.6560	0.2600	0.0170	0.4250
358.15	86.30	0.2090	0.4650	0.0350	0.2910
358.15	93.09	0.4000	0.3960	0.0290	0.3450
358.15	96.17	0.5710	0.3020	0.0240	0.3760

Mole fraction of Cyclohexanol (1) [ref]

Fixed			Measured
Temperature, K - Liquid mixture 1	Pressure, kPa - Liquid mixture 1	Mole fraction of Toluene (2) - Liquid mixture 1	Mole fraction of Cyclohexanol (1) - Liquid mixture 1
333.15	29.88	0.1500	0.5120
333.15	27.07	0.0810	0.5330
333.15	32.88	0.2820	0.4560
333.15	35.53	0.5430	0.3280
333.15	35.85	0.6090	0.2980
333.15	35.87	0.6560	0.2600
358.15	86.30	0.2090	0.4650
358.15	93.09	0.4000	0.3960
358.15	96.17	0.5710	0.3020

Temperature, K x Mass fraction [ref]

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

Fixed		Measured
Temperature, K - Liquid mixture 2	Mass fraction of Cyclohexanol (1) - Liquid mixture 1	Mass fraction of Toluene (2) - Liquid mixture 1	Mass fraction of Toluene (2) - Liquid mixture 2	Mass fraction of Cyclohexanol (1) - Liquid mixture 2
303.15	0.0190	0.9797	0.0018	0.0053
323.15	0.0286	0.9700	0.0043	0.0048
323.15	0.0472	0.9513	0.0047	0.0067
323.15	0.0638	0.9352	0.0044	0.0086
323.15	0.0807	0.9177	0.0046	0.0096
323.15	0.0975	0.9013	0.0046	0.0109
323.15	0.1141	0.8835	0.0050	0.0114
323.15	0.1667	0.8306	0.0064	0.0144
303.15	0.0358	0.9615	0.0014	0.0082
303.15	0.0488	0.9491	0.0015	0.0099
303.15	0.0586	0.9391	0.0017	0.0108
303.15	0.0762	0.9215	0.0017	0.0120
303.15	0.1227	0.8752	0.0019	0.0144
303.15	0.1356	0.8623	0.0020	0.0155
303.15	0.1528	0.8451	0.0023	0.0159
323.15	0.0134	0.9849	0.0039	0.0025

Sources

• Measurement and prediction of liquid-liquid equilibria in ternary systems containing water, an organic component, and cyclohexanol
• Measurement and Prediction of Vapor Liquid(-Liquid) Equilibria in Ternary Systems Containing Water, an Organic Component, and Cyclohexanol
• Determination and Correlation of Liquid-Liquid Equilibria Data for Water + Cyclohexanol + (Mesityl Oxide, Toluene, and p-Xylene) Ternary Systems at Different Temperatures