Mixture of n-Hexane + Anisole

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. n₀ - Refractive index (Na D-line) (2)
5. ρ_l - Mass density, kg/m3 (2)

Mole fraction of n-Hexane (1) [ref]

Operational condition: Temperature, K = 313.2 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Mole fraction of n-Hexane (1) - Gas
0.0630	0.7400
0.1380	0.8670
0.1950	0.9050
0.2380	0.9230
0.2840	0.9360
0.3280	0.9450
0.3880	0.9550
0.4500	0.9680
0.5460	0.9730
0.6220	0.9790
0.6810	0.9830
0.7290	0.9880
0.8120	0.9910
0.8490	0.9920
0.9010	0.9950
0.9350	0.9970

Mole fraction of n-Hexane (1) [ref]

Operational condition: Temperature, K = 313.2 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Mole fraction of n-Hexane (1) - Gas
0.0630	0.7400
0.1380	0.8670
0.1950	0.9050
0.2380	0.9230
0.2840	0.9360
0.3280	0.9450
0.3880	0.9550
0.4500	0.9680
0.5460	0.9730
0.6220	0.9790
0.6810	0.9830
0.7290	0.9880
0.8120	0.9910
0.8490	0.9920
0.9010	0.9950
0.9350	0.9970

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Anisole (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0003
293.15	0.0993	0.0003
293.15	0.1959	0.0004
293.15	0.3008	0.0004
293.15	0.3998	0.0004
293.15	0.5045	0.0005
293.15	0.5936	0.0006
293.15	0.6834	0.0006
293.15	0.7909	0.0008
293.15	0.8975	0.0009
293.15	1.0000	0.0011
298.15	0.0000	0.0003
298.15	0.0993	0.0003
298.15	0.1959	0.0003
298.15	0.3008	0.0004
298.15	0.3998	0.0004
298.15	0.5045	0.0005
298.15	0.5936	0.0005
298.15	0.6834	0.0006
298.15	0.7909	0.0007
298.15	0.8975	0.0008
298.15	1.0000	0.0010
303.15	0.0000	0.0003
303.15	0.0993	0.0003
303.15	0.1959	0.0003
303.15	0.3008	0.0004
303.15	0.3998	0.0004
303.15	0.5045	0.0004
303.15	0.5936	0.0005
303.15	0.6834	0.0006
303.15	0.7909	0.0007
303.15	0.8975	0.0008
303.15	1.0000	0.0009

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Anisole (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0003
293.15	0.0993	0.0003
293.15	0.1959	0.0004
293.15	0.3008	0.0004
293.15	0.3998	0.0004
293.15	0.5045	0.0005
293.15	0.5936	0.0006
293.15	0.6834	0.0006
293.15	0.7909	0.0008
293.15	0.8975	0.0009
293.15	1.0000	0.0011
298.15	0.0000	0.0003
298.15	0.0993	0.0003
298.15	0.1959	0.0003
298.15	0.3008	0.0004
298.15	0.3998	0.0004
298.15	0.5045	0.0005
298.15	0.5936	0.0005
298.15	0.6834	0.0006
298.15	0.7909	0.0007
298.15	0.8975	0.0008
298.15	1.0000	0.0010
303.15	0.0000	0.0003
303.15	0.0993	0.0003
303.15	0.1959	0.0003
303.15	0.3008	0.0004
303.15	0.3998	0.0004
303.15	0.5045	0.0004
303.15	0.5936	0.0005
303.15	0.6834	0.0006
303.15	0.7909	0.0007
303.15	0.8975	0.0008
303.15	1.0000	0.0009

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.2 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0630	4.40
0.1380	8.20
0.1950	10.90
0.2380	13.10
0.2840	15.30
0.3280	17.30
0.3880	20.10
0.4500	22.60
0.5460	26.80
0.6220	29.90
0.6810	31.40
0.7290	34.40
0.8120	35.50
0.8490	35.90
0.9010	37.20
0.9350	37.60
1.0000	37.90
0.0000	1.40

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.2 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0630	4.40
0.1380	8.20
0.1950	10.90
0.2380	13.10
0.2840	15.30
0.3280	17.30
0.3880	20.10
0.4500	22.60
0.5460	26.80
0.6220	29.90
0.6810	31.40
0.7290	34.40
0.8120	35.50
0.8490	35.90
0.9010	37.20
0.9350	37.60
1.0000	37.90
0.0000	1.40

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Anisole (2) - Liquid	Refractive index (Na D-line) - Liquid
293.15	0.0000	1.3759
293.15	0.0950	1.3873
293.15	0.1930	1.399
293.15	0.2880	1.4109
293.15	0.3910	1.4243
293.15	0.5121	1.4408
293.15	0.5942	1.4525
293.15	0.6780	1.4651
293.15	0.7790	1.4807
293.15	0.8810	1.497
293.15	1.0000	1.5161
298.15	0.0000	1.3732
298.15	0.0950	1.3844
298.15	0.1930	1.3952
298.15	0.2880	1.4081
298.15	0.3910	1.4217
298.15	0.5121	1.4382
298.15	0.5942	1.45
298.15	0.6780	1.4626
298.15	0.7790	1.4783
298.15	0.8810	1.4946
298.15	1.0000	1.5141
303.15	0.0000	1.3709
303.15	0.0950	1.3819
303.15	0.1930	1.3931
303.15	0.2880	1.4061
303.15	0.3910	1.4197
303.15	0.5121	1.4365
303.15	0.5942	1.4483
303.15	0.6780	1.4609
303.15	0.7790	1.4767
303.15	0.8810	1.4931
303.15	1.0000	1.5129

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Anisole (2) - Liquid	Refractive index (Na D-line) - Liquid
293.15	0.0000	1.3759
293.15	0.0950	1.3873
293.15	0.1930	1.399
293.15	0.2880	1.4109
293.15	0.3910	1.4243
293.15	0.5121	1.4408
293.15	0.5942	1.4525
293.15	0.6780	1.4651
293.15	0.7790	1.4807
293.15	0.8810	1.497
293.15	1.0000	1.5161
298.15	0.0000	1.3732
298.15	0.0950	1.3844
298.15	0.1930	1.3952
298.15	0.2880	1.4081
298.15	0.3910	1.4217
298.15	0.5121	1.4382
298.15	0.5942	1.45
298.15	0.6780	1.4626
298.15	0.7790	1.4783
298.15	0.8810	1.4946
298.15	1.0000	1.5141
303.15	0.0000	1.3709
303.15	0.0950	1.3819
303.15	0.1930	1.3931
303.15	0.2880	1.4061
303.15	0.3910	1.4197
303.15	0.5121	1.4365
303.15	0.5942	1.4483
303.15	0.6780	1.4609
303.15	0.7790	1.4767
303.15	0.8810	1.4931
303.15	1.0000	1.5129

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Anisole (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	659.5
293.15	0.0993	688.1
293.15	0.1959	716.85
293.15	0.3008	749.04
293.15	0.3998	780.42
293.15	0.5045	814.71
293.15	0.5936	844.84
293.15	0.6834	876.15
293.15	0.7909	914.94
293.15	0.8975	954.65
293.15	1.0000	993.81
298.15	0.0000	654.96
298.15	0.0993	683.56
298.15	0.1959	712.32
298.15	0.3008	744.42
298.15	0.3998	775.78
298.15	0.5045	810.08
298.15	0.5936	840.19
298.15	0.6834	871.52
298.15	0.7909	910.25
298.15	0.8975	949.92
298.15	1.0000	989.15
303.15	0.0000	650.42
303.15	0.0993	678.98
303.15	0.1959	707.69
303.15	0.3008	739.83
303.15	0.3998	771.15
303.15	0.5045	805.39
303.15	0.5936	835.52
303.15	0.6834	866.76
303.15	0.7909	905.45
303.15	0.8975	945.31
303.15	1.0000	984.42

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Anisole (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	659.5
293.15	0.0993	688.1
293.15	0.1959	716.85
293.15	0.3008	749.04
293.15	0.3998	780.42
293.15	0.5045	814.71
293.15	0.5936	844.84
293.15	0.6834	876.15
293.15	0.7909	914.94
293.15	0.8975	954.65
293.15	1.0000	993.81
298.15	0.0000	654.96
298.15	0.0993	683.56
298.15	0.1959	712.32
298.15	0.3008	744.42
298.15	0.3998	775.78
298.15	0.5045	810.08
298.15	0.5936	840.19
298.15	0.6834	871.52
298.15	0.7909	910.25
298.15	0.8975	949.92
298.15	1.0000	989.15
303.15	0.0000	650.42
303.15	0.0993	678.98
303.15	0.1959	707.69
303.15	0.3008	739.83
303.15	0.3998	771.15
303.15	0.5045	805.39
303.15	0.5936	835.52
303.15	0.6834	866.76
303.15	0.7909	905.45
303.15	0.8975	945.31
303.15	1.0000	984.42

Sources

• Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
• Isothermal vapor-liquid equilibrium of binary and ternary systems of anisole, hexane, and toluene and ternary system of methyl tert-butyl ether, hexane, and toluene