Mixture of Toluene + Cyclohexane

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (8)
3. Excess molar enthalpy (molar enthalpy (2)
4. P_vap - Vapor or sublimation pressure, kPa (6)
5. n₀ - Refractive index (Na D-line) (4)
6. ρ_l - Mass density, kg/m3 (12)
7. ρ_m,g - Amount density, mol/m3 (2)
8. c_sound,fluid - Speed of Sound, m/s (4)
9. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Cyclohexane (2) [ref]

Fixed		Measured
Mole fraction of Cyclohexane (2) - Liquid	Temperature, K - Gas	Mole fraction of Cyclohexane (2) - Gas
0.1854	323.20	0.4503
0.3759	323.20	0.6574
0.6076	323.20	0.8100
0.7987	323.20	0.9006
0.2013	343.20	0.4451
0.3894	343.20	0.6255
0.5947	343.20	0.7856
0.8011	343.20	0.9002
0.1986	363.20	0.4011
0.4077	363.20	0.6389
0.6013	363.20	0.7815
0.8078	363.20	0.8958

Mole fraction of Cyclohexane (2) [ref]

Fixed		Measured
Mole fraction of Cyclohexane (2) - Liquid	Temperature, K - Gas	Mole fraction of Cyclohexane (2) - Gas
0.1854	323.20	0.4503
0.3759	323.20	0.6574
0.6076	323.20	0.8100
0.7987	323.20	0.9006
0.2013	343.20	0.4451
0.3894	343.20	0.6255
0.5947	343.20	0.7856
0.8011	343.20	0.9002
0.1986	363.20	0.4011
0.4077	363.20	0.6389
0.6013	363.20	0.7815
0.8078	363.20	0.8958

Viscosity, Pa*s [ref]

Operational conditions:

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

Mole fraction of Toluene (1) - Liquid	Viscosity, Pa*s - Liquid
0.0721	0.0009
0.1813	0.0008
0.2798	0.0007
0.3613	0.0007
0.4416	0.0006
0.6003	0.0006
0.6784	0.0005
0.7615	0.0005
0.8396	0.0005
0.9202	0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Toluene (1) - Liquid	Viscosity, Pa*s - Liquid
303.15	0.0999	0.0007
303.15	0.2003	0.0007
303.15	0.3000	0.0006
303.15	0.3999	0.0006
303.15	0.5000	0.0006
303.15	0.6000	0.0005
303.15	0.6999	0.0005
303.15	0.7998	0.0005
303.15	0.9000	0.0005
308.15	0.0999	0.0007
308.15	0.2003	0.0006
308.15	0.3000	0.0006
308.15	0.3999	0.0006
308.15	0.5000	0.0005
308.15	0.6000	0.0005
308.15	0.6999	0.0005
308.15	0.7998	0.0005
308.15	0.9000	0.0005
313.15	0.0999	0.0006
313.15	0.2003	0.0006
313.15	0.3000	0.0005
313.15	0.3999	0.0005
313.15	0.5000	0.0005
313.15	0.6000	0.0005
313.15	0.6999	0.0005
313.15	0.7998	0.0005
313.15	0.9000	0.0005
318.15	0.0999	0.0006
318.15	0.2003	0.0005
318.15	0.3000	0.0005
318.15	0.3999	0.0005
318.15	0.5000	0.0005
318.15	0.6000	0.0005
318.15	0.6999	0.0005
318.15	0.7998	0.0004
318.15	0.9000	0.0004
323.15	0.0999	0.0006
323.15	0.2003	0.0005
323.15	0.3000	0.0005
323.15	0.3999	0.0005
323.15	0.5000	0.0004
323.15	0.6000	0.0004
323.15	0.6999	0.0004
323.15	0.7998	0.0004
323.15	0.9000	0.0004

Viscosity, Pa*s [ref]

Operational conditions:

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

Mole fraction of Toluene (1) - Liquid	Viscosity, Pa*s - Liquid
0.0407	0.0008
0.2018	0.0007
0.2798	0.0007
0.3613	0.0006
0.4416	0.0006
0.6003	0.0006
0.6784	0.0006
0.7615	0.0005
0.8396	0.0005
0.9202	0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0007
283.15	0.0958	0.0007
283.15	0.1960	0.0007
283.15	0.2986	0.0007
283.15	0.3988	0.0007
283.15	0.4974	0.0007
283.15	0.5989	0.0008
283.15	0.6977	0.0008
283.15	0.7998	0.0009
283.15	0.8994	0.0010
283.15	1.0000	0.0012
293.15	0.0000	0.0006
293.15	0.0958	0.0006
293.15	0.1960	0.0006
293.15	0.2986	0.0006
293.15	0.3988	0.0006
293.15	0.4974	0.0006
293.15	0.5989	0.0007
293.15	0.6977	0.0007
293.15	0.7998	0.0008
293.15	0.8994	0.0008
293.15	1.0000	0.0010
303.15	0.0000	0.0005
303.15	0.0958	0.0005
303.15	0.1960	0.0005
303.15	0.2986	0.0005
303.15	0.3988	0.0006
303.15	0.4974	0.0006
303.15	0.5989	0.0006
303.15	0.6977	0.0006
303.15	0.7998	0.0007
303.15	0.8994	0.0007
303.15	1.0000	0.0008
313.15	0.0000	0.0005
313.15	0.0958	0.0005
313.15	0.1960	0.0005
313.15	0.2986	0.0005
313.15	0.3988	0.0005
313.15	0.4974	0.0005
313.15	0.5989	0.0005
313.15	0.6977	0.0006
313.15	0.7998	0.0006
313.15	0.8994	0.0006
313.15	1.0000	0.0007
323.15	0.0000	0.0004
323.15	0.0958	0.0004
323.15	0.1960	0.0004
323.15	0.2986	0.0004
323.15	0.3988	0.0004
323.15	0.4974	0.0005
323.15	0.5989	0.0005
323.15	0.6977	0.0005
323.15	0.7998	0.0005
323.15	0.8994	0.0006
323.15	1.0000	0.0006

Viscosity, Pa*s [ref]

Operational conditions:

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

Mole fraction of Toluene (1) - Liquid	Viscosity, Pa*s - Liquid
0.0721	0.0009
0.1813	0.0008
0.2798	0.0007
0.3613	0.0007
0.4416	0.0006
0.6003	0.0006
0.6784	0.0005
0.7615	0.0005
0.8396	0.0005
0.9202	0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Toluene (1) - Liquid	Viscosity, Pa*s - Liquid
303.15	0.0999	0.0007
303.15	0.2003	0.0007
303.15	0.3000	0.0006
303.15	0.3999	0.0006
303.15	0.5000	0.0006
303.15	0.6000	0.0005
303.15	0.6999	0.0005
303.15	0.7998	0.0005
303.15	0.9000	0.0005
308.15	0.0999	0.0007
308.15	0.2003	0.0006
308.15	0.3000	0.0006
308.15	0.3999	0.0006
308.15	0.5000	0.0005
308.15	0.6000	0.0005
308.15	0.6999	0.0005
308.15	0.7998	0.0005
308.15	0.9000	0.0005
313.15	0.0999	0.0006
313.15	0.2003	0.0006
313.15	0.3000	0.0005
313.15	0.3999	0.0005
313.15	0.5000	0.0005
313.15	0.6000	0.0005
313.15	0.6999	0.0005
313.15	0.7998	0.0005
313.15	0.9000	0.0005
318.15	0.0999	0.0006
318.15	0.2003	0.0005
318.15	0.3000	0.0005
318.15	0.3999	0.0005
318.15	0.5000	0.0005
318.15	0.6000	0.0005
318.15	0.6999	0.0005
318.15	0.7998	0.0004
318.15	0.9000	0.0004
323.15	0.0999	0.0006
323.15	0.2003	0.0005
323.15	0.3000	0.0005
323.15	0.3999	0.0005
323.15	0.5000	0.0004
323.15	0.6000	0.0004
323.15	0.6999	0.0004
323.15	0.7998	0.0004
323.15	0.9000	0.0004

Viscosity, Pa*s [ref]

Operational conditions:

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

Mole fraction of Toluene (1) - Liquid	Viscosity, Pa*s - Liquid
0.0407	0.0008
0.2018	0.0007
0.2798	0.0007
0.3613	0.0006
0.4416	0.0006
0.6003	0.0006
0.6784	0.0006
0.7615	0.0005
0.8396	0.0005
0.9202	0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Viscosity, Pa*s - Liquid
283.15	0.0000	0.0007
283.15	0.0958	0.0007
283.15	0.1960	0.0007
283.15	0.2986	0.0007
283.15	0.3988	0.0007
283.15	0.4974	0.0007
283.15	0.5989	0.0008
283.15	0.6977	0.0008
283.15	0.7998	0.0009
283.15	0.8994	0.0010
283.15	1.0000	0.0012
293.15	0.0000	0.0006
293.15	0.0958	0.0006
293.15	0.1960	0.0006
293.15	0.2986	0.0006
293.15	0.3988	0.0006
293.15	0.4974	0.0006
293.15	0.5989	0.0007
293.15	0.6977	0.0007
293.15	0.7998	0.0008
293.15	0.8994	0.0008
293.15	1.0000	0.0010
303.15	0.0000	0.0005
303.15	0.0958	0.0005
303.15	0.1960	0.0005
303.15	0.2986	0.0005
303.15	0.3988	0.0006
303.15	0.4974	0.0006
303.15	0.5989	0.0006
303.15	0.6977	0.0006
303.15	0.7998	0.0007
303.15	0.8994	0.0007
303.15	1.0000	0.0008
313.15	0.0000	0.0005
313.15	0.0958	0.0005
313.15	0.1960	0.0005
313.15	0.2986	0.0005
313.15	0.3988	0.0005
313.15	0.4974	0.0005
313.15	0.5989	0.0005
313.15	0.6977	0.0006
313.15	0.7998	0.0006
313.15	0.8994	0.0006
313.15	1.0000	0.0007
323.15	0.0000	0.0004
323.15	0.0958	0.0004
323.15	0.1960	0.0004
323.15	0.2986	0.0004
323.15	0.3988	0.0004
323.15	0.4974	0.0005
323.15	0.5989	0.0005
323.15	0.6977	0.0005
323.15	0.7998	0.0005
323.15	0.8994	0.0006
323.15	1.0000	0.0006

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Cyclohexane (2) - Liquid	Temperature, K - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0000	298.15	0.0000
0.0000	313.15	0.0000
0.0491	313.15	0.1039
0.0492	298.15	0.1099
0.1003	313.15	0.2015
0.1004	298.15	0.2132
0.1496	313.15	0.2871
0.1497	298.15	0.3044
0.1990	313.15	0.3604
0.1991	298.15	0.3807
0.2485	313.15	0.4238
0.2486	298.15	0.4499
0.2980	313.15	0.4801
0.2981	298.15	0.5066
0.3477	313.15	0.5242
0.3479	298.15	0.5510
0.3974	313.15	0.5589
0.3976	298.15	0.5887
0.4493	298.15	0.6138
0.4493	313.15	0.5828
0.4992	298.15	0.6244
0.4992	313.15	0.5942
0.5493	298.15	0.6246
0.5493	313.15	0.5933
0.5974	313.15	0.5832
0.5975	298.15	0.6135
0.6476	313.15	0.5591
0.6478	298.15	0.5886
0.6979	313.15	0.5221
0.6981	298.15	0.5501
0.7483	313.15	0.4721
0.7485	298.15	0.4952
0.7989	313.15	0.4092
0.7990	298.15	0.4292
0.8496	298.15	0.3466
0.8496	313.15	0.3295
0.9003	298.15	0.2446
0.9003	313.15	0.2353
0.9491	298.15	0.1333
0.9491	313.15	0.1272
1.0000	298.15	0.0000
1.0000	313.15	0.0000

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Mole fraction of Cyclohexane (2) - Liquid	Temperature, K - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0000	298.15	0.0000
0.0000	313.15	0.0000
0.0491	313.15	0.1039
0.0492	298.15	0.1099
0.1003	313.15	0.2015
0.1004	298.15	0.2132
0.1496	313.15	0.2871
0.1497	298.15	0.3044
0.1990	313.15	0.3604
0.1991	298.15	0.3807
0.2485	313.15	0.4238
0.2486	298.15	0.4499
0.2980	313.15	0.4801
0.2981	298.15	0.5066
0.3477	313.15	0.5242
0.3479	298.15	0.5510
0.3974	313.15	0.5589
0.3976	298.15	0.5887
0.4493	298.15	0.6138
0.4493	313.15	0.5828
0.4992	298.15	0.6244
0.4992	313.15	0.5942
0.5493	298.15	0.6246
0.5493	313.15	0.5933
0.5974	313.15	0.5832
0.5975	298.15	0.6135
0.6476	313.15	0.5591
0.6478	298.15	0.5886
0.6979	313.15	0.5221
0.6981	298.15	0.5501
0.7483	313.15	0.4721
0.7485	298.15	0.4952
0.7989	313.15	0.4092
0.7990	298.15	0.4292
0.8496	298.15	0.3466
0.8496	313.15	0.3295
0.9003	298.15	0.2446
0.9003	313.15	0.2353
0.9491	298.15	0.1333
0.9491	313.15	0.1272
1.0000	298.15	0.0000
1.0000	313.15	0.0000

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Toluene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.3183	20.53
0.6735	15.12

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Cyclohexane (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1854	323.20	18.40
0.3759	323.20	23.40
0.6076	323.20	28.10
0.7987	323.20	31.90
0.2013	343.20	39.90
0.3894	343.20	48.40
0.5947	343.20	56.10
0.8011	343.20	64.20
0.1986	363.20	73.90
0.4077	363.20	91.30
0.6013	363.20	106.10
0.8078	363.20	118.40

Vapor or sublimation pressure, kPa [ref]

Operational condition: Mole fraction = 0.8026 (Liquid)

Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
303.15	8.50
308.15	10.60
313.15	13.10
323.15	19.40
333.15	28.10
343.15	39.70
352.15	53.30
365.65	80.50

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of Toluene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.3183	20.53
0.6735	15.12

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Cyclohexane (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1854	323.20	18.40
0.3759	323.20	23.40
0.6076	323.20	28.10
0.7987	323.20	31.90
0.2013	343.20	39.90
0.3894	343.20	48.40
0.5947	343.20	56.10
0.8011	343.20	64.20
0.1986	363.20	73.90
0.4077	363.20	91.30
0.6013	363.20	106.10
0.8078	363.20	118.40

Vapor or sublimation pressure, kPa [ref]

Operational condition: Mole fraction = 0.8026 (Liquid)

Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
303.15	8.50
308.15	10.60
313.15	13.10
323.15	19.40
333.15	28.10
343.15	39.70
352.15	53.30
365.65	80.50

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Cyclohexane (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.4851
0.0377	1.4821
0.0967	1.4776
0.1945	1.4701
0.2433	1.4662
0.3985	1.4547
0.5672	1.4428
0.5965	1.4407
0.7019	1.4336
0.7958	1.4276
0.9011	1.421
0.9500	1.4181
1.0000	1.4151

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0000	1.5028
283.15	0.0484	1.4988
283.15	0.0990	1.4948
283.15	0.1997	1.4868
283.15	0.2973	1.4792
283.15	0.3975	1.4717
283.15	0.4999	1.4642
283.15	0.5881	1.458
283.15	0.6990	1.4505
283.15	0.7985	1.4441
283.15	0.8961	1.4379
283.15	0.9497	1.4349
298.15	0.0000	1.494
298.15	0.0484	1.4902
298.15	0.0990	1.4861
298.15	0.1997	1.4783
298.15	0.2973	1.4707
298.15	0.3975	1.4632
298.15	0.4999	1.4558
298.15	0.5881	1.4496
298.15	0.6990	1.4422
298.15	0.7985	1.4358
298.15	0.8961	1.4297
298.15	0.9497	1.4266
298.15	1.0000	1.4236

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Cyclohexane (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.4851
0.0377	1.4821
0.0967	1.4776
0.1945	1.4701
0.2433	1.4662
0.3985	1.4547
0.5672	1.4428
0.5965	1.4407
0.7019	1.4336
0.7958	1.4276
0.9011	1.421
0.9500	1.4181
1.0000	1.4151

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Refractive index (Na D-line) - Liquid
283.15	0.0000	1.5028
283.15	0.0484	1.4988
283.15	0.0990	1.4948
283.15	0.1997	1.4868
283.15	0.2973	1.4792
283.15	0.3975	1.4717
283.15	0.4999	1.4642
283.15	0.5881	1.458
283.15	0.6990	1.4505
283.15	0.7985	1.4441
283.15	0.8961	1.4379
283.15	0.9497	1.4349
298.15	0.0000	1.494
298.15	0.0484	1.4902
298.15	0.0990	1.4861
298.15	0.1997	1.4783
298.15	0.2973	1.4707
298.15	0.3975	1.4632
298.15	0.4999	1.4558
298.15	0.5881	1.4496
298.15	0.6990	1.4422
298.15	0.7985	1.4358
298.15	0.8961	1.4297
298.15	0.9497	1.4266
298.15	1.0000	1.4236

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Toluene (1) - Liquid	Mass density, kg/m3 - Liquid
0.0721	777.43
0.1813	784.63
0.2798	791.6
0.3613	799.02
0.4416	806.0
0.6003	820.17
0.6784	827.33
0.7615	834.61
0.8396	843.41
0.9202	853.16

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Toluene (1) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0999	775.7
303.15	0.2003	783.3
303.15	0.3000	791.2
303.15	0.3999	799.7
303.15	0.5000	808.6
303.15	0.6000	817.6
303.15	0.6999	827.0
303.15	0.7998	836.8
303.15	0.9000	847.2
308.15	0.0999	771.0
308.15	0.2003	778.7
308.15	0.3000	786.6
308.15	0.3999	795.1
308.15	0.5000	804.0
308.15	0.6000	813.0
308.15	0.6999	822.4
308.15	0.7998	832.2
308.15	0.9000	842.5
313.15	0.0999	766.4
313.15	0.2003	774.1
313.15	0.3000	782.0
313.15	0.3999	790.5
313.15	0.5000	799.4
313.15	0.6000	808.4
313.15	0.6999	817.7
313.15	0.7998	827.5
313.15	0.9000	837.8
318.15	0.0999	761.6
318.15	0.2003	769.3
318.15	0.3000	777.3
318.15	0.3999	785.8
318.15	0.5000	794.7
318.15	0.6000	803.7
318.15	0.6999	813.1
318.15	0.7998	822.8
318.15	0.9000	833.1
323.15	0.0999	756.8
323.15	0.2003	764.5
323.15	0.3000	772.6
323.15	0.3999	781.1
323.15	0.5000	790.0
323.15	0.6000	799.0
323.15	0.6999	808.4
323.15	0.7998	818.1
323.15	0.9000	828.3

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Toluene (1) - Liquid	Mass density, kg/m3 - Liquid
0.0407	776.48
0.2018	788.44
0.2798	794.63
0.3613	801.33
0.4416	808.17
0.6003	822.4
0.6784	829.75
0.7615	837.82
0.8396	845.63
0.9202	853.94

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Cyclohexane (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	848.2
0.0377	844.4
0.0967	838.2
0.1945	828.5
0.2433	823.4
0.3985	808.6
0.5672	793.4
0.5965	790.9
0.7019	781.9
0.7958	774.4
0.9011	766.5
0.9500	763.0
1.0000	759.6

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	876.1
283.15	0.0958	866.15
283.15	0.1960	855.85
283.15	0.2986	846.0
283.15	0.3988	836.5
283.15	0.4974	827.65
283.15	0.5989	818.8
283.15	0.6977	810.1
283.15	0.7998	802.5
283.15	0.8994	794.8
283.15	1.0000	787.95
293.15	0.0000	866.75
293.15	0.0958	856.9
293.15	0.1960	846.6
293.15	0.2986	836.7
293.15	0.3988	827.2
293.15	0.4974	818.35
293.15	0.5989	809.4
293.15	0.6977	800.7
293.15	0.7998	793.1
293.15	0.8994	785.5
293.15	1.0000	778.7
303.15	0.0000	857.48
303.15	0.0958	847.5
303.15	0.1960	837.2
303.15	0.2986	827.3
303.15	0.3988	817.8
303.15	0.4974	808.9
303.15	0.5989	800.0
303.15	0.6977	791.3
303.15	0.7998	783.65
303.15	0.8994	776.1
303.15	1.0000	769.2
313.15	0.0000	848.08
313.15	0.0958	838.15
313.15	0.1960	827.8
313.15	0.2986	817.9
313.15	0.3988	808.4
313.15	0.4974	799.45
313.15	0.5989	790.5
313.15	0.6977	781.8
313.15	0.7998	774.15
313.15	0.8994	766.5
313.15	1.0000	759.65
323.15	0.0000	838.7
323.15	0.0958	828.65
323.15	0.1960	818.35
323.15	0.2986	808.45
323.15	0.3988	798.9
323.15	0.4974	789.95
323.15	0.5989	781.0
323.15	0.6977	772.25
323.15	0.7998	764.5
323.15	0.8994	756.9
323.15	1.0000	749.9

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	876.1
283.15	0.0484	871.0
283.15	0.0990	865.8
283.15	0.1997	855.8
283.15	0.2973	846.1
283.15	0.3975	836.6
283.15	0.4999	827.3
283.15	0.5881	819.6
283.15	0.6990	810.3
283.15	0.7985	802.4
283.15	0.8961	795.1
283.15	0.9497	791.3
298.15	0.0000	862.2
298.15	0.0484	857.2
298.15	0.0990	852.0
298.15	0.1997	842.0
298.15	0.2973	832.3
298.15	0.3975	822.8
298.15	0.4999	813.4
298.15	0.5881	805.7
298.15	0.6990	796.4
298.15	0.7985	788.4
298.15	0.8961	781.1
298.15	0.9497	777.4
298.15	1.0000	773.9

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Toluene (1) - Liquid	Mass density, kg/m3 - Liquid
0.0721	777.43
0.1813	784.63
0.2798	791.6
0.3613	799.02
0.4416	806.0
0.6003	820.17
0.6784	827.33
0.7615	834.61
0.8396	843.41
0.9202	853.16

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Toluene (1) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0999	775.7
303.15	0.2003	783.3
303.15	0.3000	791.2
303.15	0.3999	799.7
303.15	0.5000	808.6
303.15	0.6000	817.6
303.15	0.6999	827.0
303.15	0.7998	836.8
303.15	0.9000	847.2
308.15	0.0999	771.0
308.15	0.2003	778.7
308.15	0.3000	786.6
308.15	0.3999	795.1
308.15	0.5000	804.0
308.15	0.6000	813.0
308.15	0.6999	822.4
308.15	0.7998	832.2
308.15	0.9000	842.5
313.15	0.0999	766.4
313.15	0.2003	774.1
313.15	0.3000	782.0
313.15	0.3999	790.5
313.15	0.5000	799.4
313.15	0.6000	808.4
313.15	0.6999	817.7
313.15	0.7998	827.5
313.15	0.9000	837.8
318.15	0.0999	761.6
318.15	0.2003	769.3
318.15	0.3000	777.3
318.15	0.3999	785.8
318.15	0.5000	794.7
318.15	0.6000	803.7
318.15	0.6999	813.1
318.15	0.7998	822.8
318.15	0.9000	833.1
323.15	0.0999	756.8
323.15	0.2003	764.5
323.15	0.3000	772.6
323.15	0.3999	781.1
323.15	0.5000	790.0
323.15	0.6000	799.0
323.15	0.6999	808.4
323.15	0.7998	818.1
323.15	0.9000	828.3

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Toluene (1) - Liquid	Mass density, kg/m3 - Liquid
0.0407	776.48
0.2018	788.44
0.2798	794.63
0.3613	801.33
0.4416	808.17
0.6003	822.4
0.6784	829.75
0.7615	837.82
0.8396	845.63
0.9202	853.94

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Cyclohexane (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	848.2
0.0377	844.4
0.0967	838.2
0.1945	828.5
0.2433	823.4
0.3985	808.6
0.5672	793.4
0.5965	790.9
0.7019	781.9
0.7958	774.4
0.9011	766.5
0.9500	763.0
1.0000	759.6

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	876.1
283.15	0.0958	866.15
283.15	0.1960	855.85
283.15	0.2986	846.0
283.15	0.3988	836.5
283.15	0.4974	827.65
283.15	0.5989	818.8
283.15	0.6977	810.1
283.15	0.7998	802.5
283.15	0.8994	794.8
283.15	1.0000	787.95
293.15	0.0000	866.75
293.15	0.0958	856.9
293.15	0.1960	846.6
293.15	0.2986	836.7
293.15	0.3988	827.2
293.15	0.4974	818.35
293.15	0.5989	809.4
293.15	0.6977	800.7
293.15	0.7998	793.1
293.15	0.8994	785.5
293.15	1.0000	778.7
303.15	0.0000	857.48
303.15	0.0958	847.5
303.15	0.1960	837.2
303.15	0.2986	827.3
303.15	0.3988	817.8
303.15	0.4974	808.9
303.15	0.5989	800.0
303.15	0.6977	791.3
303.15	0.7998	783.65
303.15	0.8994	776.1
303.15	1.0000	769.2
313.15	0.0000	848.08
313.15	0.0958	838.15
313.15	0.1960	827.8
313.15	0.2986	817.9
313.15	0.3988	808.4
313.15	0.4974	799.45
313.15	0.5989	790.5
313.15	0.6977	781.8
313.15	0.7998	774.15
313.15	0.8994	766.5
313.15	1.0000	759.65
323.15	0.0000	838.7
323.15	0.0958	828.65
323.15	0.1960	818.35
323.15	0.2986	808.45
323.15	0.3988	798.9
323.15	0.4974	789.95
323.15	0.5989	781.0
323.15	0.6977	772.25
323.15	0.7998	764.5
323.15	0.8994	756.9
323.15	1.0000	749.9

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Mass density, kg/m3 - Liquid
283.15	0.0000	876.1
283.15	0.0484	871.0
283.15	0.0990	865.8
283.15	0.1997	855.8
283.15	0.2973	846.1
283.15	0.3975	836.6
283.15	0.4999	827.3
283.15	0.5881	819.6
283.15	0.6990	810.3
283.15	0.7985	802.4
283.15	0.8961	795.1
283.15	0.9497	791.3
298.15	0.0000	862.2
298.15	0.0484	857.2
298.15	0.0990	852.0
298.15	0.1997	842.0
298.15	0.2973	832.3
298.15	0.3975	822.8
298.15	0.4999	813.4
298.15	0.5881	805.7
298.15	0.6990	796.4
298.15	0.7985	788.4
298.15	0.8961	781.1
298.15	0.9497	777.4
298.15	1.0000	773.9

Amount density, mol/m3 [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Cyclohexane (2) - Gas	Amount density, mol/m3 - Gas
566.40	0.6443	3248.0
580.70	0.2977	3338.0
562.90	0.7371	2600.0
579.80	0.3237	2593.0
567.40	0.5980	3984.0
576.00	0.3626	3881.0
561.60	0.5758	1881.0
548.20	0.5648	5277.0
567.80	0.6127	3772.0
583.60	0.2264	3217.0
562.50	0.7783	2734.0
581.60	0.2758	3260.0
561.90	0.7108	2215.0
572.50	0.3473	4578.0
569.10	0.5967	3016.0
565.30	0.6733	3240.0
561.10	0.5721	1813.0

Amount density, mol/m3 [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Cyclohexane (2) - Gas	Amount density, mol/m3 - Gas
566.40	0.6443	3248.0
580.70	0.2977	3338.0
562.90	0.7371	2600.0
579.80	0.3237	2593.0
567.40	0.5980	3984.0
576.00	0.3626	3881.0
561.60	0.5758	1881.0
548.20	0.5648	5277.0
567.80	0.6127	3772.0
583.60	0.2264	3217.0
562.50	0.7783	2734.0
581.60	0.2758	3260.0
561.90	0.7108	2215.0
572.50	0.3473	4578.0
569.10	0.5967	3016.0
565.30	0.6733	3240.0
561.10	0.5721	1813.0

Speed of sound, m/s [ref]

Operational conditions:

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

Mole fraction of Cyclohexane (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1240.9
0.0377	1236.8
0.0967	1230.0
0.1945	1220.1
0.2433	1215.4
0.3985	1202.3
0.5672	1191.4
0.5965	1189.8
0.7019	1185.1
0.7958	1182.2
0.9011	1181.2
0.9500	1180.9
1.0000	1181.7

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0000	1371.0
283.15	0.0484	1365.0
283.15	0.0990	1360.0
283.15	0.1997	1351.0
283.15	0.2973	1344.0
283.15	0.3975	1337.0
283.15	0.4999	1331.0
283.15	0.5881	1328.0
283.15	0.6990	1325.0
283.15	0.7985	1324.0
283.15	0.8961	1325.0
283.15	0.9497	1327.0
283.15	1.0000	1329.0
298.15	0.0000	1305.0
298.15	0.0484	1300.0
298.15	0.0990	1294.0
298.15	0.1997	1285.0
298.15	0.2973	1276.0
298.15	0.3975	1269.0
298.15	0.4999	1263.0
298.15	0.5881	1258.0
298.15	0.6990	1254.0
298.15	0.7985	1252.0
298.15	0.8961	1252.0
298.15	0.9497	1253.0
298.15	1.0000	1255.0

Speed of sound, m/s [ref]

Operational conditions:

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

Mole fraction of Cyclohexane (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1240.9
0.0377	1236.8
0.0967	1230.0
0.1945	1220.1
0.2433	1215.4
0.3985	1202.3
0.5672	1191.4
0.5965	1189.8
0.7019	1185.1
0.7958	1182.2
0.9011	1181.2
0.9500	1180.9
1.0000	1181.7

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane (2) - Liquid	Speed of sound, m/s - Liquid
283.15	0.0000	1371.0
283.15	0.0484	1365.0
283.15	0.0990	1360.0
283.15	0.1997	1351.0
283.15	0.2973	1344.0
283.15	0.3975	1337.0
283.15	0.4999	1331.0
283.15	0.5881	1328.0
283.15	0.6990	1325.0
283.15	0.7985	1324.0
283.15	0.8961	1325.0
283.15	0.9497	1327.0
283.15	1.0000	1329.0
298.15	0.0000	1305.0
298.15	0.0484	1300.0
298.15	0.0990	1294.0
298.15	0.1997	1285.0
298.15	0.2973	1276.0
298.15	0.3975	1269.0
298.15	0.4999	1263.0
298.15	0.5881	1258.0
298.15	0.6990	1254.0
298.15	0.7985	1252.0
298.15	0.8961	1252.0
298.15	0.9497	1253.0
298.15	1.0000	1255.0

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	383.60
0.0295	382.12
0.0515	380.72
0.0987	378.33
0.1838	374.31
0.2964	369.86
0.3968	366.50
0.4981	363.57
0.5994	361.15
0.6985	358.97
0.8018	356.94
0.9000	355.27
0.9530	354.42
0.9703	354.19
0.9839	353.84
1.0000	353.82

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	383.60
0.0295	382.12
0.0515	380.72
0.0987	378.33
0.1838	374.31
0.2964	369.86
0.3968	366.50
0.4981	363.57
0.5994	361.15
0.6985	358.97
0.8018	356.94
0.9000	355.27
0.9530	354.42
0.9703	354.19
0.9839	353.84
1.0000	353.82

Sources

• Experimental investigation of the vapour-liquid equilibrium of binary and ternary mixtures containing dibutyl ether (DBE), cyclohexane and toluene at 313.15 K
• Plotting of phase (vapor-liquid) transition surface near the critical point out of data from isochoric experiment. Experimental procedure
• Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter
• Volumetric and viscometric studies of molecular interaction of the ternary system toluene (1) + cyclohexane (2) + n-hexane (3) at 298.15K
• A new analysis method for improving collection of vapor-liquid equilibrium (VLE) data of binary mixtures using differential scanning calorimetry (DSC)
• Vapor Liquid Equilibria for (n-Hexane, n-Octane, Cyclohexane, or 2,3-Dimethylpentane) + Toluene + {[4empy][Tf2N] (0.3) + [emim][DCA] (0.7)} Mixed Ionic Liquids
• Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
• Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
• Viscosities and Excess Molar Volumes of the Ternary System Toluene (1) + Cyclohexane (2) + Pentane (3) at 298.15 K
• Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes and Aromatic Compounds at T = 313.15 K
• Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
• Density, Speed of Sound, and Refractive Index of the Binary Systems Cyclohexane (1) or Methylcyclohexane (1) or Cyclo-octane (1) with Benzene (2), Toluene (2), and Ethylbenzene (2) at Two Temperatures