Mixture of 1-Hexene + n-Propyl acetate

Datasets

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

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

Operational conditions:

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

Mole fraction of n-Propyl acetate (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0943	0.2592
0.2122	0.4753
0.3238	0.5897
0.4180	0.6306
0.4609	0.6367
0.4822	0.6349
0.5032	0.6329
0.5241	0.6278
0.5449	0.6202
0.6178	0.5811
0.7186	0.4889
0.8117	0.3656
0.9076	0.1988

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

Operational conditions:

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

Mole fraction of n-Propyl acetate (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0943	0.2592
0.2122	0.4753
0.3238	0.5897
0.4180	0.6306
0.4609	0.6367
0.4822	0.6349
0.5032	0.6329
0.5241	0.6278
0.5449	0.6202
0.6178	0.5811
0.7186	0.4889
0.8117	0.3656
0.9076	0.1988

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Propyl acetate (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
273.15	0.0000	7.69
273.15	0.1540	6.80
273.15	0.2625	6.22
273.15	0.4090	5.52
273.15	0.5290	4.86
273.15	0.6682	4.07
273.15	0.8082	2.99
273.15	0.9362	1.76
273.15	1.0000	1.01
283.15	0.0000	12.64
283.15	0.1540	11.18
283.15	0.2625	10.27
283.15	0.4090	9.13
283.15	0.5290	8.06
283.15	0.6682	6.77
283.15	0.8082	5.05
283.15	0.9362	3.10
283.15	1.0000	1.91
293.15	0.0000	19.98
293.15	0.1540	17.68
293.15	0.2625	16.27
293.15	0.4090	14.51
293.15	0.5290	12.85
293.15	0.6682	10.84
293.15	0.8082	8.20
293.15	0.9362	5.23
293.15	1.0000	3.43
298.15	0.0000	24.77
298.15	0.1540	21.95
298.15	0.2625	20.22
298.15	0.4090	18.04
298.15	0.5290	16.01
298.15	0.6682	13.54
298.15	0.8082	10.30
298.15	0.9362	6.70
298.15	1.0000	4.51
303.15	0.0000	30.46
303.15	0.1540	27.03
303.15	0.2625	24.91
303.15	0.4090	22.25
303.15	0.5290	19.78
303.15	0.6682	16.76
303.15	0.8082	12.84
303.15	0.9362	8.49
303.15	1.0000	5.87
313.15	0.0000	44.98
313.15	0.1540	40.07
313.15	0.2625	36.95
313.15	0.4090	33.08
313.15	0.5290	29.50
313.15	0.6682	25.12
313.15	0.8082	19.50
313.15	0.9362	13.32
313.15	1.0000	9.65
323.15	0.0000	64.60
323.15	0.1540	57.82
323.15	0.2625	53.31
323.15	0.4090	47.81
323.15	0.5290	42.78
323.15	0.6682	36.62
323.15	0.8082	28.78
323.15	0.9362	20.25
323.15	1.0000	15.25
333.15	0.0000	90.44
333.15	0.1540	81.41
333.15	0.2625	75.00
333.15	0.4090	67.39
333.15	0.5290	60.50
333.15	0.6682	52.05
333.15	0.8082	41.41
333.15	0.9362	29.94
333.15	1.0000	23.33
343.15	0.0000	123.79
343.15	0.1540	112.09
343.15	0.2625	103.16
343.15	0.4090	92.87
343.15	0.5290	83.64
343.15	0.6682	72.31
343.15	0.8082	58.23
343.15	0.9362	43.19
343.15	1.0000	34.64
353.15	0.0000	165.99
353.15	0.1540	151.29
353.15	0.2625	139.03
353.15	0.4090	125.38
353.15	0.5290	113.27
353.15	0.6682	98.42
353.15	0.8082	80.20
353.15	0.9362	60.88
353.15	1.0000	50.07
363.15	0.0000	218.50
363.15	0.1540	200.49
363.15	0.2625	183.92
363.15	0.4090	166.15
363.15	0.5290	150.57
363.15	0.6682	131.47
363.15	0.8082	108.37
363.15	0.9362	84.08
363.15	1.0000	70.64

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of n-Propyl acetate (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
273.15	0.0000	7.69
273.15	0.1540	6.80
273.15	0.2625	6.22
273.15	0.4090	5.52
273.15	0.5290	4.86
273.15	0.6682	4.07
273.15	0.8082	2.99
273.15	0.9362	1.76
273.15	1.0000	1.01
283.15	0.0000	12.64
283.15	0.1540	11.18
283.15	0.2625	10.27
283.15	0.4090	9.13
283.15	0.5290	8.06
283.15	0.6682	6.77
283.15	0.8082	5.05
283.15	0.9362	3.10
283.15	1.0000	1.91
293.15	0.0000	19.98
293.15	0.1540	17.68
293.15	0.2625	16.27
293.15	0.4090	14.51
293.15	0.5290	12.85
293.15	0.6682	10.84
293.15	0.8082	8.20
293.15	0.9362	5.23
293.15	1.0000	3.43
298.15	0.0000	24.77
298.15	0.1540	21.95
298.15	0.2625	20.22
298.15	0.4090	18.04
298.15	0.5290	16.01
298.15	0.6682	13.54
298.15	0.8082	10.30
298.15	0.9362	6.70
298.15	1.0000	4.51
303.15	0.0000	30.46
303.15	0.1540	27.03
303.15	0.2625	24.91
303.15	0.4090	22.25
303.15	0.5290	19.78
303.15	0.6682	16.76
303.15	0.8082	12.84
303.15	0.9362	8.49
303.15	1.0000	5.87
313.15	0.0000	44.98
313.15	0.1540	40.07
313.15	0.2625	36.95
313.15	0.4090	33.08
313.15	0.5290	29.50
313.15	0.6682	25.12
313.15	0.8082	19.50
313.15	0.9362	13.32
313.15	1.0000	9.65
323.15	0.0000	64.60
323.15	0.1540	57.82
323.15	0.2625	53.31
323.15	0.4090	47.81
323.15	0.5290	42.78
323.15	0.6682	36.62
323.15	0.8082	28.78
323.15	0.9362	20.25
323.15	1.0000	15.25
333.15	0.0000	90.44
333.15	0.1540	81.41
333.15	0.2625	75.00
333.15	0.4090	67.39
333.15	0.5290	60.50
333.15	0.6682	52.05
333.15	0.8082	41.41
333.15	0.9362	29.94
333.15	1.0000	23.33
343.15	0.0000	123.79
343.15	0.1540	112.09
343.15	0.2625	103.16
343.15	0.4090	92.87
343.15	0.5290	83.64
343.15	0.6682	72.31
343.15	0.8082	58.23
343.15	0.9362	43.19
343.15	1.0000	34.64
353.15	0.0000	165.99
353.15	0.1540	151.29
353.15	0.2625	139.03
353.15	0.4090	125.38
353.15	0.5290	113.27
353.15	0.6682	98.42
353.15	0.8082	80.20
353.15	0.9362	60.88
353.15	1.0000	50.07
363.15	0.0000	218.50
363.15	0.1540	200.49
363.15	0.2625	183.92
363.15	0.4090	166.15
363.15	0.5290	150.57
363.15	0.6682	131.47
363.15	0.8082	108.37
363.15	0.9362	84.08
363.15	1.0000	70.64

Sources

• Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)