Mixture of Acetic acid, propyl ester + 3-Hexyne

Datasets

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

Mole fraction of Acetic acid, propyl ester (1) [ref]

Fixed		Measured
Mole fraction of Acetic acid, propyl ester (1) - Liquid	Temperature, K - Liquid	Mole fraction of Acetic acid, propyl ester (1) - Gas
0.0000	273.15	0.0000
0.0000	283.15	0.0000
0.0000	293.15	0.0000
0.0000	298.15	0.0000
0.0000	303.15	0.0000
0.0000	313.15	0.0000
0.0000	323.15	0.0000
0.0000	333.15	0.0000
0.0000	343.15	0.0000
0.0000	353.15	0.0000
0.0000	363.15	0.0000
0.1507	273.15	0.0694
0.1507	283.15	0.0722
0.1507	293.15	0.0750
0.1507	298.15	0.0764
0.1507	303.15	0.0779
0.1507	313.15	0.0808
0.1507	323.15	0.0838
0.1507	333.15	0.0869
0.1507	343.15	0.0900
0.1507	353.15	0.0932
0.1507	363.15	0.0965
0.3753	273.15	0.1742
0.3753	283.15	0.1863
0.3753	293.15	0.1976
0.3753	298.15	0.2029
0.3753	303.15	0.2080
0.3753	313.15	0.2177
0.3753	323.15	0.2268
0.3753	333.15	0.2352
0.3753	343.15	0.2429
0.3753	353.15	0.2502
0.3753	363.15	0.2570
0.4302	273.15	0.2068
0.4302	283.15	0.2200
0.4302	293.15	0.2323
0.4302	298.15	0.2381
0.4302	303.15	0.2437
0.4302	313.15	0.2542
0.4302	323.15	0.2640
0.4302	333.15	0.2732
0.4302	343.15	0.2816
0.4302	353.15	0.2895
0.4302	363.15	0.2968
0.6409	273.15	0.3605
0.6409	283.15	0.3768
0.6409	293.15	0.3921
0.6409	298.15	0.3994
0.6409	303.15	0.4066
0.6409	313.15	0.4203
0.6409	323.15	0.4333
0.6409	333.15	0.4457
0.6409	343.15	0.4574
0.6409	353.15	0.4687
0.6409	363.15	0.4734
0.7608	273.15	0.4817
0.7608	283.15	0.5005
0.7608	293.15	0.5180
0.7608	298.15	0.5264
0.7608	303.15	0.5345
0.7608	313.15	0.5500
0.7608	323.15	0.5646
0.7608	333.15	0.5785
0.7608	343.15	0.5917
0.7608	353.15	0.6042
0.7608	363.15	0.6162
0.8645	273.15	0.6370
0.8645	283.15	0.6555
0.8645	293.15	0.6723
0.8645	298.15	0.6801
0.8645	303.15	0.6875
0.8645	313.15	0.7014
0.8645	323.15	0.7142
0.8645	333.15	0.7260
0.8645	343.15	0.7369
0.8645	353.15	0.7471
0.8645	363.15	0.7567
1.0000	273.15	1.0000
1.0000	283.15	1.0000
1.0000	293.15	1.0000
1.0000	298.15	1.0000
1.0000	303.15	1.0000
1.0000	313.15	1.0000
1.0000	323.15	1.0000
1.0000	333.15	1.0000
1.0000	343.15	1.0000
1.0000	353.15	1.0000
1.0000	363.15	1.0000

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

Operational conditions:

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

Mole fraction of Acetic acid, propyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0968	0.0440
0.2020	0.0777
0.3025	0.1126
0.4063	0.1426
0.4979	0.1579
0.5956	0.1475
0.7045	0.1118
0.7995	0.0763
0.8928	0.0422

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Acetic acid, propyl ester (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	273.15	2.92
0.0000	283.15	5.23
0.0000	293.15	8.90
0.0000	298.15	11.41
0.0000	303.15	14.48
0.0000	313.15	22.67
0.0000	323.15	34.28
0.0000	333.15	50.29
0.0000	343.15	71.78
0.0000	353.15	99.99
0.0000	363.15	136.24
0.1507	273.15	2.75
0.1507	283.15	4.87
0.1507	293.15	8.24
0.1507	298.15	10.54
0.1507	303.15	13.36
0.1507	313.15	20.87
0.1507	323.15	31.53
0.1507	333.15	46.25
0.1507	343.15	66.08
0.1507	353.15	92.17
0.1507	363.15	125.83
0.3753	273.15	2.36
0.3753	283.15	4.22
0.3753	293.15	7.18
0.3753	298.15	9.22
0.3753	303.15	11.71
0.3753	313.15	18.40
0.3753	323.15	27.95
0.3753	333.15	41.23
0.3753	343.15	59.21
0.3753	353.15	83.02
0.3753	363.15	113.90
0.4302	273.15	2.27
0.4302	283.15	4.05
0.4302	293.15	6.91
0.4302	298.15	8.88
0.4302	303.15	11.29
0.4302	313.15	17.77
0.4302	323.15	27.05
0.4302	333.15	39.96
0.4302	343.15	57.47
0.4302	353.15	80.68
0.4302	363.15	110.83
0.6409	273.15	1.86
0.6409	283.15	3.36
0.6409	293.15	5.79
0.6409	298.15	7.48
0.6409	303.15	9.55
0.6409	313.15	15.15
0.6409	323.15	23.24
0.6409	333.15	34.57
0.6409	343.15	50.04
0.6409	353.15	70.66
0.6409	363.15	97.60
0.7608	273.15	1.61
0.7608	283.15	2.94
0.7608	293.15	5.12
0.7608	298.15	6.63
0.7608	303.15	8.50
0.7608	313.15	13.59
0.7608	323.15	20.96
0.7608	333.15	31.33
0.7608	343.15	45.55
0.7608	353.15	64.56
0.7608	363.15	89.46
0.8645	273.15	1.37
0.8645	283.15	2.52
0.8645	293.15	4.42
0.8645	298.15	5.76
0.8645	303.15	7.41
0.8645	313.15	11.94
0.8645	323.15	18.57
0.8645	333.15	27.98
0.8645	343.15	40.99
0.8645	353.15	58.56
0.8645	363.15	81.75
1.0000	273.15	1.01
1.0000	283.15	1.91
1.0000	293.15	3.43
1.0000	298.15	4.51
1.0000	303.15	5.87
1.0000	313.15	9.65
1.0000	323.15	15.25
1.0000	333.15	23.33
1.0000	343.15	34.64
1.0000	353.15	50.07
1.0000	363.15	70.64

Sources

• Isothermal vapor-liquid equilibria and excess enthalpies of binary mixtures of propyl ethanoate + 1-hexyne, +2-hexyne, +3-hexyne