Mixture of Ethanol + Nonane

Datasets

1. Mole fraction (2)
2. Excess molar enthalpy (molar enthalpy (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)

Mole fraction of Ethanol (1) [ref]

Fixed		Measured
Mole fraction of Ethanol (1) - Liquid	Temperature, K - Liquid	Mole fraction of Ethanol (1) - Gas
0.0000	323.21	0.0000
0.0610	323.21	0.8750
0.0830	323.21	0.9000
0.1140	323.21	0.9100
0.2080	323.21	0.9120
0.2880	323.21	0.9150
0.3300	323.21	0.9160
0.3960	323.21	0.9170
0.4950	323.21	0.9180
0.6020	323.21	0.9250
0.7570	323.21	0.9300
0.8000	323.21	0.9310
0.8920	323.21	0.9400
0.9300	323.21	0.9490
0.9560	323.21	0.9600
0.9720	323.21	0.9710
1.0000	323.21	1.0000
0.0000	333.21	0.0000
0.0720	333.21	0.8840
0.0940	333.21	0.8910
0.1320	333.21	0.9020
0.2100	333.21	0.9070
0.3010	333.21	0.9140
0.4130	333.21	0.9160
0.5430	333.21	0.9180
0.6090	333.21	0.9240
0.7890	333.21	0.9300
0.8370	333.21	0.9330
0.8980	333.21	0.9410
0.9300	333.21	0.9500
0.9570	333.21	0.9610
0.9720	333.21	0.9710
1.0000	333.21	1.0000
0.0000	343.21	0.0000
0.0890	343.21	0.8790
0.2160	343.21	0.9050
0.2950	343.21	0.9100
0.3740	343.21	0.9130
0.4580	343.21	0.9160
0.5080	343.21	0.9170
0.5920	343.21	0.9190
0.6290	343.21	0.9200
0.6730	343.21	0.9220
0.7140	343.21	0.9230
0.7500	343.21	0.9250
0.7810	343.21	0.9270
0.7990	343.21	0.9280
0.8080	343.21	0.9290
0.8190	343.21	0.9300
0.8410	343.21	0.9320
0.8640	343.21	0.9350
0.8780	343.21	0.9380
0.8990	343.21	0.9420
0.9190	343.21	0.9470
0.9370	343.21	0.9530
0.9530	343.21	0.9600
0.9670	343.21	0.9690
0.9790	343.21	0.9780
0.9890	343.21	0.9870
1.0000	343.21	1.0000

Mole fraction of Ethanol (1) [ref]

Fixed		Measured
Mole fraction of Ethanol (1) - Liquid	Temperature, K - Liquid	Mole fraction of Ethanol (1) - Gas
0.0000	323.21	0.0000
0.0610	323.21	0.8750
0.0830	323.21	0.9000
0.1140	323.21	0.9100
0.2080	323.21	0.9120
0.2880	323.21	0.9150
0.3300	323.21	0.9160
0.3960	323.21	0.9170
0.4950	323.21	0.9180
0.6020	323.21	0.9250
0.7570	323.21	0.9300
0.8000	323.21	0.9310
0.8920	323.21	0.9400
0.9300	323.21	0.9490
0.9560	323.21	0.9600
0.9720	323.21	0.9710
1.0000	323.21	1.0000
0.0000	333.21	0.0000
0.0720	333.21	0.8840
0.0940	333.21	0.8910
0.1320	333.21	0.9020
0.2100	333.21	0.9070
0.3010	333.21	0.9140
0.4130	333.21	0.9160
0.5430	333.21	0.9180
0.6090	333.21	0.9240
0.7890	333.21	0.9300
0.8370	333.21	0.9330
0.8980	333.21	0.9410
0.9300	333.21	0.9500
0.9570	333.21	0.9610
0.9720	333.21	0.9710
1.0000	333.21	1.0000
0.0000	343.21	0.0000
0.0890	343.21	0.8790
0.2160	343.21	0.9050
0.2950	343.21	0.9100
0.3740	343.21	0.9130
0.4580	343.21	0.9160
0.5080	343.21	0.9170
0.5920	343.21	0.9190
0.6290	343.21	0.9200
0.6730	343.21	0.9220
0.7140	343.21	0.9230
0.7500	343.21	0.9250
0.7810	343.21	0.9270
0.7990	343.21	0.9280
0.8080	343.21	0.9290
0.8190	343.21	0.9300
0.8410	343.21	0.9320
0.8640	343.21	0.9350
0.8780	343.21	0.9380
0.8990	343.21	0.9420
0.9190	343.21	0.9470
0.9370	343.21	0.9530
0.9530	343.21	0.9600
0.9670	343.21	0.9690
0.9790	343.21	0.9780
0.9890	343.21	0.9870
1.0000	343.21	1.0000

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

Operational conditions:

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

Mole fraction of Ethanol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0507	0.3640
0.1378	0.5520
0.2453	0.6540
0.4164	0.7040
0.5022	0.6770
0.5860	0.6520
0.6518	0.6300
0.6895	0.5980
0.7490	0.5420
0.7877	0.5020
0.8433	0.4190
0.8715	0.3760
0.9065	0.2990
0.9296	0.2400
0.9562	0.1620

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

Operational conditions:

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

Mole fraction of Ethanol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0507	0.3640
0.1378	0.5520
0.2453	0.6540
0.4164	0.7040
0.5022	0.6770
0.5860	0.6520
0.6518	0.6300
0.6895	0.5980
0.7490	0.5420
0.7877	0.5020
0.8433	0.4190
0.8715	0.3760
0.9065	0.2990
0.9296	0.2400
0.9562	0.1620

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethanol (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	323.21	2.42
0.0610	323.21	19.21
0.0830	323.21	23.28
0.1140	323.21	26.65
0.2080	323.21	28.10
0.2880	323.21	28.56
0.3300	323.21	28.64
0.3960	323.21	28.68
0.4950	323.21	28.74
0.6020	323.21	28.73
0.7570	323.21	29.15
0.8000	323.21	29.24
0.8920	323.21	29.50
0.9300	323.21	29.61
0.9560	323.21	29.77
0.9720	323.21	29.80
1.0000	323.21	29.58
0.0000	333.21	4.03
0.0720	333.21	33.87
0.0940	333.21	35.83
0.1320	333.21	39.43
0.2100	333.21	43.51
0.3010	333.21	44.85
0.4130	333.21	45.12
0.5430	333.21	45.35
0.6090	333.21	45.48
0.7890	333.21	46.11
0.8370	333.21	46.30
0.8980	333.21	46.78
0.9300	333.21	46.95
0.9570	333.21	47.06
0.9720	333.21	47.15
1.0000	333.21	47.04
0.0000	343.21	6.33
0.0890	343.21	50.49
0.2160	343.21	61.94
0.2950	343.21	64.67
0.3740	343.21	66.24
0.4580	343.21	67.51
0.5080	343.21	67.98
0.5920	343.21	68.83
0.6290	343.21	69.16
0.6730	343.21	69.53
0.7140	343.21	69.83
0.7500	343.21	70.20
0.7810	343.21	70.54
0.7990	343.21	70.69
0.8080	343.21	70.80
0.8190	343.21	70.91
0.8410	343.21	71.16
0.8640	343.21	71.53
0.8780	343.21	71.68
0.8990	343.21	71.93
0.9190	343.21	72.19
0.9370	343.21	72.39
0.9530	343.21	72.58
0.9670	343.21	72.65
0.9790	343.21	72.65
0.9890	343.21	72.58
1.0000	343.21	72.39

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethanol (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	323.21	2.42
0.0610	323.21	19.21
0.0830	323.21	23.28
0.1140	323.21	26.65
0.2080	323.21	28.10
0.2880	323.21	28.56
0.3300	323.21	28.64
0.3960	323.21	28.68
0.4950	323.21	28.74
0.6020	323.21	28.73
0.7570	323.21	29.15
0.8000	323.21	29.24
0.8920	323.21	29.50
0.9300	323.21	29.61
0.9560	323.21	29.77
0.9720	323.21	29.80
1.0000	323.21	29.58
0.0000	333.21	4.03
0.0720	333.21	33.87
0.0940	333.21	35.83
0.1320	333.21	39.43
0.2100	333.21	43.51
0.3010	333.21	44.85
0.4130	333.21	45.12
0.5430	333.21	45.35
0.6090	333.21	45.48
0.7890	333.21	46.11
0.8370	333.21	46.30
0.8980	333.21	46.78
0.9300	333.21	46.95
0.9570	333.21	47.06
0.9720	333.21	47.15
1.0000	333.21	47.04
0.0000	343.21	6.33
0.0890	343.21	50.49
0.2160	343.21	61.94
0.2950	343.21	64.67
0.3740	343.21	66.24
0.4580	343.21	67.51
0.5080	343.21	67.98
0.5920	343.21	68.83
0.6290	343.21	69.16
0.6730	343.21	69.53
0.7140	343.21	69.83
0.7500	343.21	70.20
0.7810	343.21	70.54
0.7990	343.21	70.69
0.8080	343.21	70.80
0.8190	343.21	70.91
0.8410	343.21	71.16
0.8640	343.21	71.53
0.8780	343.21	71.68
0.8990	343.21	71.93
0.9190	343.21	72.19
0.9370	343.21	72.39
0.9530	343.21	72.58
0.9670	343.21	72.65
0.9790	343.21	72.65
0.9890	343.21	72.58
1.0000	343.21	72.39

Sources

• Vapor-Liquid Equilibrium Measurements of Ethanol and n-Nonane or n-Decane Binary Mixtures with Large Relative Volatility
• Excess Molar Enthalpies of Ternary and Binary Mixtures Containing 2-Methoxy-2-Methylpropane, Ethanol, and Nonane