Mixture of n-Hexane + Ethanol

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (2)
3. Excess molar enthalpy (molar enthalpy (2)
4. P_c - Critical pressure, kPa (2)
5. n₀ - Refractive index (Na D-line) (2)
6. ρ_l - Mass density, kg/m3 (4)
7. c_sound,fluid - Speed of Sound, m/s (2)
8. γ - Surface tension liquid-gas, N/m (2)
9. T_boil - Boiling temperature at pressure P, K (2)
10. T_c - Critical temperature, K (2)
11. Binary diffusion coefficient, m2/s (2)
12. Vapor Liquid Equilibrium at Constant Pressure
13. Vapor Liquid Equilibrium at Constant Temperature (2)
14. Excess molar volume, m3/mol (2)

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Mole fraction of Ethanol (2) - Gas
0.9987	0.9444
0.9975	0.8271
0.9940	0.7782
0.9931	0.7355
0.9616	0.6382
0.9408	0.5734
0.9210	0.5339
0.9052	0.5202
0.8657	0.4965
0.8282	0.4818
0.7868	0.4533
0.6554	0.4333
0.5533	0.4177
0.3842	0.3842
0.3076	0.3679
0.2009	0.3288
0.1348	0.2586
0.0880	0.1944
0.0462	0.1137

Mole fraction of Ethanol (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Mole fraction of Ethanol (2) - Gas
0.9987	0.9444
0.9975	0.8271
0.9940	0.7782
0.9931	0.7355
0.9616	0.6382
0.9408	0.5734
0.9210	0.5339
0.9052	0.5202
0.8657	0.4965
0.8282	0.4818
0.7868	0.4533
0.6554	0.4333
0.5533	0.4177
0.3842	0.3842
0.3076	0.3679
0.2009	0.3288
0.1348	0.2586
0.0880	0.1944
0.0462	0.1137

Viscosity, Pa*s [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.0000	293.15	0.0003
0.0000	298.15	0.0003
0.1010	273.15	0.0004
0.1010	275.65	0.0004
0.1010	278.15	0.0003
0.1010	280.65	0.0003
0.1010	283.15	0.0003
0.1010	285.65	0.0003
0.1010	288.15	0.0003
0.1010	290.65	0.0003
0.1010	293.15	0.0003
0.1010	295.65	0.0003
0.1010	298.15	0.0003
0.1980	273.15	0.0004
0.1980	275.65	0.0004
0.1980	278.15	0.0004
0.1980	280.65	0.0004
0.1980	283.15	0.0004
0.1980	285.65	0.0004
0.1980	288.15	0.0003
0.1980	290.65	0.0003
0.1980	293.15	0.0003
0.1980	295.65	0.0003
0.1980	298.15	0.0003
0.3020	273.15	0.0005
0.3020	275.65	0.0004
0.3020	278.15	0.0004
0.3020	280.65	0.0004
0.3020	283.15	0.0004
0.3020	285.65	0.0004
0.3020	288.15	0.0004
0.3020	290.65	0.0004
0.3020	293.15	0.0004
0.3020	295.65	0.0003
0.3020	298.15	0.0003
0.4010	273.15	0.0005
0.4010	275.65	0.0005
0.4010	278.15	0.0005
0.4010	280.65	0.0005
0.4010	283.15	0.0005
0.4010	285.65	0.0005
0.4010	288.15	0.0004
0.4010	290.65	0.0004
0.4010	293.15	0.0004
0.4010	295.65	0.0004
0.4010	298.15	0.0004
0.4960	273.15	0.0006
0.4960	275.65	0.0006
0.4960	278.15	0.0006
0.4960	280.65	0.0006
0.4960	283.15	0.0006
0.4960	285.65	0.0005
0.4960	288.15	0.0005
0.4960	290.65	0.0005
0.4960	293.15	0.0004
0.4960	295.65	0.0004
0.4960	298.15	0.0004
0.6000	273.15	0.0008
0.6000	275.65	0.0007
0.6000	278.15	0.0007
0.6000	280.65	0.0007
0.6000	283.15	0.0007
0.6000	285.65	0.0006
0.6000	288.15	0.0006
0.6000	290.65	0.0006
0.6000	293.15	0.0006
0.6000	295.65	0.0005
0.6000	298.15	0.0005
0.7010	273.15	0.0009
0.7010	275.65	0.0009
0.7010	278.15	0.0008
0.7010	280.65	0.0008
0.7010	283.15	0.0008
0.7010	285.65	0.0007
0.7010	288.15	0.0007
0.7010	290.65	0.0007
0.7010	293.15	0.0006
0.7010	295.65	0.0006
0.7010	298.15	0.0006
0.7930	273.15	0.0011
0.7930	275.65	0.0010
0.7930	278.15	0.0010
0.7930	280.65	0.0010
0.7930	283.15	0.0009
0.7930	285.65	0.0009
0.7930	288.15	0.0008
0.7930	290.65	0.0008
0.7930	293.15	0.0008
0.7930	295.65	0.0007
0.7930	298.15	0.0007
0.9010	273.15	0.0014
0.9010	275.65	0.0013
0.9010	278.15	0.0012
0.9010	280.65	0.0012
0.9010	283.15	0.0011
0.9010	285.65	0.0011
0.9010	288.15	0.0010
0.9010	290.65	0.0010
0.9010	293.15	0.0009
0.9010	295.65	0.0009
0.9010	298.15	0.0009
1.0000	293.15	0.0012
1.0000	298.15	0.0011

Viscosity, Pa*s [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.0000	293.15	0.0003
0.0000	298.15	0.0003
0.1010	273.15	0.0004
0.1010	275.65	0.0004
0.1010	278.15	0.0003
0.1010	280.65	0.0003
0.1010	283.15	0.0003
0.1010	285.65	0.0003
0.1010	288.15	0.0003
0.1010	290.65	0.0003
0.1010	293.15	0.0003
0.1010	295.65	0.0003
0.1010	298.15	0.0003
0.1980	273.15	0.0004
0.1980	275.65	0.0004
0.1980	278.15	0.0004
0.1980	280.65	0.0004
0.1980	283.15	0.0004
0.1980	285.65	0.0004
0.1980	288.15	0.0003
0.1980	290.65	0.0003
0.1980	293.15	0.0003
0.1980	295.65	0.0003
0.1980	298.15	0.0003
0.3020	273.15	0.0005
0.3020	275.65	0.0004
0.3020	278.15	0.0004
0.3020	280.65	0.0004
0.3020	283.15	0.0004
0.3020	285.65	0.0004
0.3020	288.15	0.0004
0.3020	290.65	0.0004
0.3020	293.15	0.0004
0.3020	295.65	0.0003
0.3020	298.15	0.0003
0.4010	273.15	0.0005
0.4010	275.65	0.0005
0.4010	278.15	0.0005
0.4010	280.65	0.0005
0.4010	283.15	0.0005
0.4010	285.65	0.0005
0.4010	288.15	0.0004
0.4010	290.65	0.0004
0.4010	293.15	0.0004
0.4010	295.65	0.0004
0.4010	298.15	0.0004
0.4960	273.15	0.0006
0.4960	275.65	0.0006
0.4960	278.15	0.0006
0.4960	280.65	0.0006
0.4960	283.15	0.0006
0.4960	285.65	0.0005
0.4960	288.15	0.0005
0.4960	290.65	0.0005
0.4960	293.15	0.0004
0.4960	295.65	0.0004
0.4960	298.15	0.0004
0.6000	273.15	0.0008
0.6000	275.65	0.0007
0.6000	278.15	0.0007
0.6000	280.65	0.0007
0.6000	283.15	0.0007
0.6000	285.65	0.0006
0.6000	288.15	0.0006
0.6000	290.65	0.0006
0.6000	293.15	0.0006
0.6000	295.65	0.0005
0.6000	298.15	0.0005
0.7010	273.15	0.0009
0.7010	275.65	0.0009
0.7010	278.15	0.0008
0.7010	280.65	0.0008
0.7010	283.15	0.0008
0.7010	285.65	0.0007
0.7010	288.15	0.0007
0.7010	290.65	0.0007
0.7010	293.15	0.0006
0.7010	295.65	0.0006
0.7010	298.15	0.0006
0.7930	273.15	0.0011
0.7930	275.65	0.0010
0.7930	278.15	0.0010
0.7930	280.65	0.0010
0.7930	283.15	0.0009
0.7930	285.65	0.0009
0.7930	288.15	0.0008
0.7930	290.65	0.0008
0.7930	293.15	0.0008
0.7930	295.65	0.0007
0.7930	298.15	0.0007
0.9010	273.15	0.0014
0.9010	275.65	0.0013
0.9010	278.15	0.0012
0.9010	280.65	0.0012
0.9010	283.15	0.0011
0.9010	285.65	0.0011
0.9010	288.15	0.0010
0.9010	290.65	0.0010
0.9010	293.15	0.0009
0.9010	295.65	0.0009
0.9010	298.15	0.0009
1.0000	293.15	0.0012
1.0000	298.15	0.0011

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

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0544	0.2800
0.1056	0.4149
0.1538	0.4796
0.1994	0.5273
0.2426	0.5503
0.2835	0.5687
0.3592	0.5795
0.4277	0.5678
0.4596	0.5607
0.4900	0.5637
0.5191	0.5564
0.5992	0.5122
0.6472	0.4843
0.7125	0.4453
0.8064	0.3546
0.8997	0.2240
0.9528	0.1216

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

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0544	0.2800
0.1056	0.4149
0.1538	0.4796
0.1994	0.5273
0.2426	0.5503
0.2835	0.5687
0.3592	0.5795
0.4277	0.5678
0.4596	0.5607
0.4900	0.5637
0.5191	0.5564
0.5992	0.5122
0.6472	0.4843
0.7125	0.4453
0.8064	0.3546
0.8997	0.2240
0.9528	0.1216

Critical pressure, kPa [ref]

Mole fraction of Ethanol (2) - Liquid	Critical pressure, kPa - Liquid
0.0000	3030.00
0.1026	3387.00
0.2253	3703.00
0.3200	3920.00
0.4380	4170.00
0.5251	4317.00
0.6207	4601.00
0.7120	4853.00
0.8203	5240.00
0.9113	5651.00
1.0000	6135.00

Critical pressure, kPa [ref]

Mole fraction of Ethanol (2) - Liquid	Critical pressure, kPa - Liquid
0.0000	3030.00
0.1026	3387.00
0.2253	3703.00
0.3200	3920.00
0.4380	4170.00
0.5251	4317.00
0.6207	4601.00
0.7120	4853.00
0.8203	5240.00
0.9113	5651.00
1.0000	6135.00

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Refractive index (Na D-line) - Liquid
293.15	0.0000	1.3749
293.15	0.0469	1.3743
293.15	0.1003	1.3737
293.15	0.2004	1.3726
293.15	0.3080	1.3714
293.15	0.3987	1.3704
293.15	0.4999	1.3691
293.15	0.6038	1.3678
293.15	0.6769	1.3666
293.15	0.7992	1.3647
293.15	0.9007	1.363
293.15	0.9505	1.3621
293.15	1.0000	1.3614
298.15	0.0000	1.3722
298.15	0.0469	1.3716
298.15	0.1003	1.371
298.15	0.2004	1.3698
298.15	0.3080	1.3687
298.15	0.3987	1.3677
298.15	0.4999	1.3665
298.15	0.6038	1.3652
298.15	0.6769	1.3642
298.15	0.7992	1.3623
298.15	0.9007	1.3608
298.15	0.9505	1.36
298.15	1.0000	1.3593
303.15	0.0000	1.3694
303.15	0.0469	1.3688
303.15	0.1003	1.3682
303.15	0.2004	1.3671
303.15	0.3080	1.3659
303.15	0.3987	1.3649
303.15	0.4999	1.3638
303.15	0.6038	1.3626
303.15	0.6769	1.3616
303.15	0.7992	1.36
303.15	0.9007	1.3586
303.15	0.9505	1.3579
303.15	1.0000	1.3573

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Refractive index (Na D-line) - Liquid
293.15	0.0000	1.3749
293.15	0.0469	1.3743
293.15	0.1003	1.3737
293.15	0.2004	1.3726
293.15	0.3080	1.3714
293.15	0.3987	1.3704
293.15	0.4999	1.3691
293.15	0.6038	1.3678
293.15	0.6769	1.3666
293.15	0.7992	1.3647
293.15	0.9007	1.363
293.15	0.9505	1.3621
293.15	1.0000	1.3614
298.15	0.0000	1.3722
298.15	0.0469	1.3716
298.15	0.1003	1.371
298.15	0.2004	1.3698
298.15	0.3080	1.3687
298.15	0.3987	1.3677
298.15	0.4999	1.3665
298.15	0.6038	1.3652
298.15	0.6769	1.3642
298.15	0.7992	1.3623
298.15	0.9007	1.3608
298.15	0.9505	1.36
298.15	1.0000	1.3593
303.15	0.0000	1.3694
303.15	0.0469	1.3688
303.15	0.1003	1.3682
303.15	0.2004	1.3671
303.15	0.3080	1.3659
303.15	0.3987	1.3649
303.15	0.4999	1.3638
303.15	0.6038	1.3626
303.15	0.6769	1.3616
303.15	0.7992	1.36
303.15	0.9007	1.3586
303.15	0.9505	1.3579
303.15	1.0000	1.3573

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	659.5
293.15	0.0469	661.5
293.15	0.1003	664.4
293.15	0.2004	670.7
293.15	0.3080	678.7
293.15	0.3987	686.5
293.15	0.4999	696.7
293.15	0.6038	709.1
293.15	0.6769	719.3
293.15	0.7992	739.9
293.15	0.9007	761.8
293.15	0.9505	774.9
293.15	1.0000	789.3
298.15	0.0000	654.9
298.15	0.0469	656.9
298.15	0.1003	659.8
298.15	0.2004	666.0
298.15	0.3080	674.1
298.15	0.3987	681.9
298.15	0.4999	692.1
298.15	0.6038	704.6
298.15	0.6769	714.8
298.15	0.7992	735.5
298.15	0.9007	757.5
298.15	0.9505	770.6
298.15	1.0000	785.1
303.15	0.0000	650.4
303.15	0.0469	652.2
303.15	0.1003	655.1
303.15	0.2004	661.4
303.15	0.3080	669.4
303.15	0.3987	677.2
303.15	0.4999	687.4
303.15	0.6038	700.0
303.15	0.6769	710.2
303.15	0.7992	731.0
303.15	0.9007	753.1
303.15	0.9505	766.2
303.15	1.0000	780.7

Mass density, kg/m3 [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	293.15	659.8
0.0000	298.15	655.3
0.1010	273.15	688.8
0.1010	275.65	686.5
0.1010	278.15	684.3
0.1010	280.65	682.0
0.1010	283.15	679.8
0.1010	285.65	677.5
0.1010	288.15	675.2
0.1010	290.65	672.8
0.1010	293.15	670.5
0.1010	295.65	668.2
0.1010	298.15	665.9
0.1980	273.15	694.5
0.1980	275.65	692.3
0.1980	278.15	690.0
0.1980	280.65	687.8
0.1980	283.15	685.5
0.1980	285.65	683.2
0.1980	288.15	680.9
0.1980	290.65	678.6
0.1980	293.15	676.2
0.1980	295.65	673.9
0.1980	298.15	671.5
0.3020	273.15	702.0
0.3020	275.65	699.7
0.3020	278.15	697.5
0.3020	280.65	695.2
0.3020	283.15	692.9
0.3020	285.65	690.6
0.3020	288.15	688.3
0.3020	290.65	686.0
0.3020	293.15	683.7
0.3020	295.65	681.4
0.3020	298.15	679.0
0.4010	273.15	712.1
0.4010	275.65	709.8
0.4010	278.15	707.6
0.4010	280.65	704.9
0.4010	283.15	702.7
0.4010	285.65	700.4
0.4010	288.15	698.1
0.4010	290.65	695.8
0.4010	293.15	693.5
0.4010	295.65	691.1
0.4010	298.15	688.8
0.4960	273.15	721.4
0.4960	275.65	719.2
0.4960	278.15	716.9
0.4960	280.65	714.7
0.4960	283.15	712.4
0.4960	285.65	710.1
0.4960	288.15	707.9
0.4960	290.65	705.5
0.4960	293.15	703.2
0.4960	295.65	700.9
0.4960	298.15	688.6
0.6000	273.15	732.7
0.6000	275.65	730.5
0.6000	278.15	728.3
0.6000	280.65	726.1
0.6000	283.15	723.8
0.6000	285.65	721.5
0.6000	288.15	719.3
0.6000	290.65	717.0
0.6000	293.15	714.7
0.6000	295.65	712.4
0.6000	298.15	710.1
0.7010	273.15	744.1
0.7010	275.65	741.9
0.7010	278.15	739.7
0.7010	280.65	737.4
0.7010	283.15	735.2
0.7010	285.65	733.0
0.7010	288.15	730.8
0.7010	290.65	728.5
0.7010	293.15	726.2
0.7010	295.65	724.0
0.7010	298.15	721.7
0.7930	273.15	760.4
0.7930	275.65	758.3
0.7930	278.15	756.1
0.7930	280.65	753.9
0.7930	283.15	751.7
0.7930	285.65	749.5
0.7930	288.15	747.3
0.7930	290.65	745.1
0.7930	293.15	742.8
0.7930	295.65	740.6
0.7930	298.15	738.3
0.9010	273.15	781.1
0.9010	275.65	779.0
0.9010	278.15	776.8
0.9010	280.65	774.7
0.9010	283.15	772.5
0.9010	285.65	770.4
0.9010	288.15	768.2
0.9010	290.65	766.0
0.9010	293.15	763.9
0.9010	295.65	761.7
0.9010	298.15	759.5
1.0000	293.15	790.2
1.0000	298.15	785.9

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	659.5
293.15	0.0469	661.5
293.15	0.1003	664.4
293.15	0.2004	670.7
293.15	0.3080	678.7
293.15	0.3987	686.5
293.15	0.4999	696.7
293.15	0.6038	709.1
293.15	0.6769	719.3
293.15	0.7992	739.9
293.15	0.9007	761.8
293.15	0.9505	774.9
293.15	1.0000	789.3
298.15	0.0000	654.9
298.15	0.0469	656.9
298.15	0.1003	659.8
298.15	0.2004	666.0
298.15	0.3080	674.1
298.15	0.3987	681.9
298.15	0.4999	692.1
298.15	0.6038	704.6
298.15	0.6769	714.8
298.15	0.7992	735.5
298.15	0.9007	757.5
298.15	0.9505	770.6
298.15	1.0000	785.1
303.15	0.0000	650.4
303.15	0.0469	652.2
303.15	0.1003	655.1
303.15	0.2004	661.4
303.15	0.3080	669.4
303.15	0.3987	677.2
303.15	0.4999	687.4
303.15	0.6038	700.0
303.15	0.6769	710.2
303.15	0.7992	731.0
303.15	0.9007	753.1
303.15	0.9505	766.2
303.15	1.0000	780.7

Mass density, kg/m3 [ref]

Fixed		Measured
Mole fraction of Ethanol (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	293.15	659.8
0.0000	298.15	655.3
0.1010	273.15	688.8
0.1010	275.65	686.5
0.1010	278.15	684.3
0.1010	280.65	682.0
0.1010	283.15	679.8
0.1010	285.65	677.5
0.1010	288.15	675.2
0.1010	290.65	672.8
0.1010	293.15	670.5
0.1010	295.65	668.2
0.1010	298.15	665.9
0.1980	273.15	694.5
0.1980	275.65	692.3
0.1980	278.15	690.0
0.1980	280.65	687.8
0.1980	283.15	685.5
0.1980	285.65	683.2
0.1980	288.15	680.9
0.1980	290.65	678.6
0.1980	293.15	676.2
0.1980	295.65	673.9
0.1980	298.15	671.5
0.3020	273.15	702.0
0.3020	275.65	699.7
0.3020	278.15	697.5
0.3020	280.65	695.2
0.3020	283.15	692.9
0.3020	285.65	690.6
0.3020	288.15	688.3
0.3020	290.65	686.0
0.3020	293.15	683.7
0.3020	295.65	681.4
0.3020	298.15	679.0
0.4010	273.15	712.1
0.4010	275.65	709.8
0.4010	278.15	707.6
0.4010	280.65	704.9
0.4010	283.15	702.7
0.4010	285.65	700.4
0.4010	288.15	698.1
0.4010	290.65	695.8
0.4010	293.15	693.5
0.4010	295.65	691.1
0.4010	298.15	688.8
0.4960	273.15	721.4
0.4960	275.65	719.2
0.4960	278.15	716.9
0.4960	280.65	714.7
0.4960	283.15	712.4
0.4960	285.65	710.1
0.4960	288.15	707.9
0.4960	290.65	705.5
0.4960	293.15	703.2
0.4960	295.65	700.9
0.4960	298.15	688.6
0.6000	273.15	732.7
0.6000	275.65	730.5
0.6000	278.15	728.3
0.6000	280.65	726.1
0.6000	283.15	723.8
0.6000	285.65	721.5
0.6000	288.15	719.3
0.6000	290.65	717.0
0.6000	293.15	714.7
0.6000	295.65	712.4
0.6000	298.15	710.1
0.7010	273.15	744.1
0.7010	275.65	741.9
0.7010	278.15	739.7
0.7010	280.65	737.4
0.7010	283.15	735.2
0.7010	285.65	733.0
0.7010	288.15	730.8
0.7010	290.65	728.5
0.7010	293.15	726.2
0.7010	295.65	724.0
0.7010	298.15	721.7
0.7930	273.15	760.4
0.7930	275.65	758.3
0.7930	278.15	756.1
0.7930	280.65	753.9
0.7930	283.15	751.7
0.7930	285.65	749.5
0.7930	288.15	747.3
0.7930	290.65	745.1
0.7930	293.15	742.8
0.7930	295.65	740.6
0.7930	298.15	738.3
0.9010	273.15	781.1
0.9010	275.65	779.0
0.9010	278.15	776.8
0.9010	280.65	774.7
0.9010	283.15	772.5
0.9010	285.65	770.4
0.9010	288.15	768.2
0.9010	290.65	766.0
0.9010	293.15	763.9
0.9010	295.65	761.7
0.9010	298.15	759.5
1.0000	293.15	790.2
1.0000	298.15	785.9

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1100.0
293.15	0.0469	1095.0
293.15	0.1003	1093.0
293.15	0.2004	1091.0
293.15	0.3080	1091.0
293.15	0.3987	1092.0
293.15	0.4999	1095.0
293.15	0.6038	1099.0
293.15	0.6769	1104.0
293.15	0.7992	1117.0
293.15	0.9007	1134.0
293.15	0.9505	1145.0
293.15	1.0000	1160.0
298.15	0.0000	1078.0
298.15	0.0469	1073.0
298.15	0.1003	1071.0
298.15	0.2004	1069.0
298.15	0.3080	1069.0
298.15	0.3987	1070.0
298.15	0.4999	1073.0
298.15	0.6038	1078.0
298.15	0.6769	1084.0
298.15	0.7992	1097.0
298.15	0.9007	1115.0
298.15	0.9505	1128.0
298.15	1.0000	1143.0
303.15	0.0000	1055.0
303.15	0.0469	1050.0
303.15	0.1003	1048.0
303.15	0.2004	1046.0
303.15	0.3080	1046.0
303.15	0.3987	1048.0
303.15	0.4999	1052.0
303.15	0.6038	1058.0
303.15	0.6769	1063.0
303.15	0.7992	1078.0
303.15	0.9007	1097.0
303.15	0.9505	1110.0
303.15	1.0000	1127.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Speed of sound, m/s - Liquid
293.15	0.0000	1100.0
293.15	0.0469	1095.0
293.15	0.1003	1093.0
293.15	0.2004	1091.0
293.15	0.3080	1091.0
293.15	0.3987	1092.0
293.15	0.4999	1095.0
293.15	0.6038	1099.0
293.15	0.6769	1104.0
293.15	0.7992	1117.0
293.15	0.9007	1134.0
293.15	0.9505	1145.0
293.15	1.0000	1160.0
298.15	0.0000	1078.0
298.15	0.0469	1073.0
298.15	0.1003	1071.0
298.15	0.2004	1069.0
298.15	0.3080	1069.0
298.15	0.3987	1070.0
298.15	0.4999	1073.0
298.15	0.6038	1078.0
298.15	0.6769	1084.0
298.15	0.7992	1097.0
298.15	0.9007	1115.0
298.15	0.9505	1128.0
298.15	1.0000	1143.0
303.15	0.0000	1055.0
303.15	0.0469	1050.0
303.15	0.1003	1048.0
303.15	0.2004	1046.0
303.15	0.3080	1046.0
303.15	0.3987	1048.0
303.15	0.4999	1052.0
303.15	0.6038	1058.0
303.15	0.6769	1063.0
303.15	0.7992	1078.0
303.15	0.9007	1097.0
303.15	0.9505	1110.0
303.15	1.0000	1127.0

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
283.15	0.0855	0.0197
283.15	0.1006	0.0197
283.15	0.2107	0.0197
283.15	0.2928	0.0198
283.15	0.4128	0.0199
283.15	0.5071	0.0201
283.15	0.5909	0.0203
283.15	0.7036	0.0206
283.15	0.8032	0.0210
283.15	0.9021	0.0218
283.15	0.9320	0.0221
288.15	0.0855	0.0191
288.15	0.1006	0.0191
288.15	0.2107	0.0191
288.15	0.2928	0.0192
288.15	0.4128	0.0193
288.15	0.5071	0.0195
288.15	0.5909	0.0197
288.15	0.7036	0.0200
288.15	0.8032	0.0205
288.15	0.9021	0.0213
288.15	0.9320	0.0216
293.15	0.0855	0.0186
293.15	0.1006	0.0186
293.15	0.2107	0.0186
293.15	0.2928	0.0186
293.15	0.4128	0.0187
293.15	0.5071	0.0188
293.15	0.5909	0.0190
293.15	0.7036	0.0194
293.15	0.8032	0.0199
293.15	0.9021	0.0207
293.15	0.9320	0.0211
298.15	0.0855	0.0180
298.15	0.1006	0.0180
298.15	0.2107	0.0180
298.15	0.2928	0.0180
298.15	0.4128	0.0181
298.15	0.5071	0.0183
298.15	0.5909	0.0185
298.15	0.7036	0.0188
298.15	0.8032	0.0193
298.15	0.9021	0.0202
298.15	0.9320	0.0206
303.15	0.0855	0.0175
303.15	0.1006	0.0175
303.15	0.2107	0.0174
303.15	0.2928	0.0175
303.15	0.4128	0.0176
303.15	0.5071	0.0177
303.15	0.5909	0.0179
303.15	0.7036	0.0183
303.15	0.8032	0.0188
303.15	0.9021	0.0198
303.15	0.9320	0.0202
308.15	0.0855	0.0167
308.15	0.1006	0.0167
308.15	0.2107	0.0166
308.15	0.2928	0.0167
308.15	0.4128	0.0169
308.15	0.5071	0.0170
308.15	0.5909	0.0173
308.15	0.7036	0.0177
308.15	0.8032	0.0183
308.15	0.9021	0.0194
308.15	0.9320	0.0198
313.15	0.0855	0.0163
313.15	0.1006	0.0163
313.15	0.2107	0.0162
313.15	0.2928	0.0162
313.15	0.4128	0.0164
313.15	0.5071	0.0166
313.15	0.5909	0.0167
313.15	0.7036	0.0172
313.15	0.8032	0.0179
313.15	0.9021	0.0189
313.15	0.9320	0.0194

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
283.15	0.0855	0.0197
283.15	0.1006	0.0197
283.15	0.2107	0.0197
283.15	0.2928	0.0198
283.15	0.4128	0.0199
283.15	0.5071	0.0201
283.15	0.5909	0.0203
283.15	0.7036	0.0206
283.15	0.8032	0.0210
283.15	0.9021	0.0218
283.15	0.9320	0.0221
288.15	0.0855	0.0191
288.15	0.1006	0.0191
288.15	0.2107	0.0191
288.15	0.2928	0.0192
288.15	0.4128	0.0193
288.15	0.5071	0.0195
288.15	0.5909	0.0197
288.15	0.7036	0.0200
288.15	0.8032	0.0205
288.15	0.9021	0.0213
288.15	0.9320	0.0216
293.15	0.0855	0.0186
293.15	0.1006	0.0186
293.15	0.2107	0.0186
293.15	0.2928	0.0186
293.15	0.4128	0.0187
293.15	0.5071	0.0188
293.15	0.5909	0.0190
293.15	0.7036	0.0194
293.15	0.8032	0.0199
293.15	0.9021	0.0207
293.15	0.9320	0.0211
298.15	0.0855	0.0180
298.15	0.1006	0.0180
298.15	0.2107	0.0180
298.15	0.2928	0.0180
298.15	0.4128	0.0181
298.15	0.5071	0.0183
298.15	0.5909	0.0185
298.15	0.7036	0.0188
298.15	0.8032	0.0193
298.15	0.9021	0.0202
298.15	0.9320	0.0206
303.15	0.0855	0.0175
303.15	0.1006	0.0175
303.15	0.2107	0.0174
303.15	0.2928	0.0175
303.15	0.4128	0.0176
303.15	0.5071	0.0177
303.15	0.5909	0.0179
303.15	0.7036	0.0183
303.15	0.8032	0.0188
303.15	0.9021	0.0198
303.15	0.9320	0.0202
308.15	0.0855	0.0167
308.15	0.1006	0.0167
308.15	0.2107	0.0166
308.15	0.2928	0.0167
308.15	0.4128	0.0169
308.15	0.5071	0.0170
308.15	0.5909	0.0173
308.15	0.7036	0.0177
308.15	0.8032	0.0183
308.15	0.9021	0.0194
308.15	0.9320	0.0198
313.15	0.0855	0.0163
313.15	0.1006	0.0163
313.15	0.2107	0.0162
313.15	0.2928	0.0162
313.15	0.4128	0.0164
313.15	0.5071	0.0166
313.15	0.5909	0.0167
313.15	0.7036	0.0172
313.15	0.8032	0.0179
313.15	0.9021	0.0189
313.15	0.9320	0.0194

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.9987	350.75
0.9975	347.55
0.9940	346.15
0.9931	344.95
0.9616	342.15
0.9408	340.15
0.9210	338.65
0.9052	337.45
0.8657	336.05
0.8282	334.65
0.7868	333.85
0.6554	332.65
0.5533	332.45
0.3842	332.15
0.3076	332.45
0.2009	333.45
0.1348	334.95
0.0880	337.15
0.0462	339.05

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.9987	350.75
0.9975	347.55
0.9940	346.15
0.9931	344.95
0.9616	342.15
0.9408	340.15
0.9210	338.65
0.9052	337.45
0.8657	336.05
0.8282	334.65
0.7868	333.85
0.6554	332.65
0.5533	332.45
0.3842	332.15
0.3076	332.45
0.2009	333.45
0.1348	334.95
0.0880	337.15
0.0462	339.05

Critical temperature, K [ref]

Mole fraction of Ethanol (2) - Liquid	Critical temperature, K - Liquid
0.0000	507.90
0.1026	501.50
0.2253	496.70
0.3200	493.60
0.4380	490.60
0.5251	489.50
0.6207	490.50
0.7120	493.50
0.8203	499.40
0.9113	505.40
1.0000	514.20

Critical temperature, K [ref]

Mole fraction of Ethanol (2) - Liquid	Critical temperature, K - Liquid
0.0000	507.90
0.1026	501.50
0.2253	496.70
0.3200	493.60
0.4380	490.60
0.5251	489.50
0.6207	490.50
0.7120	493.50
0.8203	499.40
0.9113	505.40
1.0000	514.20

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0000	0.0000
0.0300	0.0000
0.1000	0.0000
0.3000	0.0000
0.5000	0.0000
0.7000	0.0000
0.9000	0.0000
0.9700	0.0000
1.0000	0.0000

Binary diffusion coefficient, m2/s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Binary diffusion coefficient, m2/s - Liquid
0.0000	0.0000
0.0300	0.0000
0.1000	0.0000
0.3000	0.0000
0.5000	0.0000
0.7000	0.0000
0.9000	0.0000
0.9700	0.0000
1.0000	0.0000

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of n-Hexane (1) - Liquid	y1[mol/mol] of n-Hexane (1) - Vapour
351.45	0.0000	0.0000
349.15	0.0100	0.0950
346.35	0.0200	0.1930
340.55	0.0600	0.3650
339.05	0.0800	0.4200
334.95	0.1520	0.5320
332.55	0.2450	0.6050
331.85	0.3330	0.6300
331.5	0.4520	0.6400
331.25	0.5880	0.6500
331.15	0.6700	0.6600
331.4	0.7250	0.6700
331.6	0.7650	0.6750
332.3	0.8980	0.7100
333.35	0.9550	0.7450
336.65	0.9900	0.8400
339.85	0.9940	0.9350
341.85	1.0000	1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 328.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of n-Hexane (1) - Liquid	y1[mol/mol] of n-Hexane (1) - Vapour
46.036	0.0110	0.1780
65.488	0.0700	0.4310
71.794	0.1000	0.4870
78.447	0.1410	0.5200
83.193	0.2060	0.5680
87.246	0.3030	0.5830
88.033	0.3320	0.5950
89.113	0.3870	0.6060
89.753	0.4090	0.6090
89.926	0.4980	0.6210
90.193	0.5370	0.6220
90.219	0.6030	0.6350
89.939	0.7240	0.6500
89.793	0.8100	0.6820
87.313	0.9000	0.7040
85.393	0.9430	0.7460
80.26	0.9610	0.8020

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 263.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of n-Hexane (1) - Liquid	y1[mol/mol] of n-Hexane (1) - Vapour
2.3065	0.0500	0.6474
3.1	0.1000	0.7441
3.504	0.1500	0.7793
3.738	0.2000	0.7978
3.884	0.2500	0.8067
3.98	0.3000	0.8124
4.04	0.3500	0.8151
4.089	0.4000	0.8184
4.126	0.4500	0.8207
4.16	0.5000	0.8221
4.189	0.5500	0.8233
4.208	0.6000	0.8248
4.22	0.6500	0.8262
4.221	0.7000	0.8275
4.213	0.7500	0.8291
4.197	0.8000	0.8323
4.157	0.8500	0.8402
4.09	0.9000	0.8566
3.99	0.9500	0.8897

Excess molar volume, m3/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0417	1.5000e-07
0.1280	2.8900e-07
0.1661	3.2700e-07
0.1998	3.5400e-07
0.2039	3.5300e-07
0.2988	3.9600e-07
0.3473	4.0600e-07
0.3985	4.0900e-07
0.3998	4.1100e-07
0.4524	4.1200e-07
0.4995	4.0800e-07
0.5596	3.9500e-07
0.5985	3.8400e-07
0.6015	3.8100e-07
0.6487	3.6500e-07
0.7029	3.3300e-07
0.7607	3.0000e-07
0.8004	2.6900e-07
0.8009	2.7000e-07
0.8508	2.1800e-07
0.8989	1.6300e-07
0.9197	1.3600e-07
0.9497	8.8000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.325 (Liquid)

Mole fraction of Ethanol (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0417	1.5000e-07
0.1280	2.8900e-07
0.1661	3.2700e-07
0.1998	3.5400e-07
0.2039	3.5300e-07
0.2988	3.9600e-07
0.3473	4.0600e-07
0.3985	4.0900e-07
0.3998	4.1100e-07
0.4524	4.1200e-07
0.4995	4.0800e-07
0.5596	3.9500e-07
0.5985	3.8400e-07
0.6015	3.8100e-07
0.6487	3.6500e-07
0.7029	3.3300e-07
0.7607	3.0000e-07
0.8004	2.6900e-07
0.8009	2.7000e-07
0.8508	2.1800e-07
0.8989	1.6300e-07
0.9197	1.3600e-07
0.9497	8.8000e-08

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Excess molar volumes and excess molar enthalpies of binary and ternary mixtures of (ethanol or 1-butanol), triethylamine and n-hexane
• Vapor-liquid equilibrium in the binary and ternary systems containing ethyl propionate, ethanol and alkane at 101.3 kPa
• Mixing properties of binary mixtures presenting azeotropes at several temperatures
• Measurement of critical temperatures and critical pressures for binary mixtures of methyl tert-butyl ether (MTBE) + alcohol and MTBE + alkane
• Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems
• Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
• Viscosity and Density of Binary Mixtures of Ethyl Alcohol with n-Alkanes (C6, C8, and C10)