Mixture of n-Hexane + 1-Propanol, 2-methyl-

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. ρ_l - Mass density, kg/m3 (2)
5. c_sound,fluid - Speed of Sound, m/s (2)

Mole fraction of n-Hexane (1) [ref]

Fixed		Measured
Mole fraction of n-Hexane (1) - Liquid	Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Gas
0.0000	303.15	0.0000
0.0101	303.15	0.3570
0.0522	303.15	0.7149
0.0821	303.15	0.8046
0.1202	303.15	0.8529
0.1930	303.15	0.8924
0.2382	303.15	0.9079
0.2823	303.15	0.9197
0.3252	303.15	0.9243
0.4142	303.15	0.9343
0.4804	303.15	0.9427
0.5423	303.15	0.9467
0.6131	303.15	0.9507
0.7373	303.15	0.9538
0.8331	303.15	0.9558
0.9273	303.15	0.9607
0.9527	303.15	0.9658
0.9802	303.15	0.9812
0.9951	303.15	0.9945
1.0000	303.15	1.0000
0.0000	323.15	0.0000
0.0091	323.15	0.2349
0.0491	323.15	0.6158
0.0831	323.15	0.7274
0.1193	323.15	0.7838
0.1940	323.15	0.8428
0.2373	323.15	0.8589
0.2832	323.15	0.8806
0.3261	323.15	0.8873
0.4152	323.15	0.9063
0.4795	323.15	0.9090
0.5432	323.15	0.9140
0.6141	323.15	0.9170
0.7363	323.15	0.9190
0.8341	323.15	0.9208
0.9263	323.15	0.9486
0.9536	323.15	0.9588
0.9792	323.15	0.9783
0.9960	323.15	0.9954
1.0000	323.15	1.0000
0.0000	343.15	0.0000
0.0070	343.15	0.1465
0.0500	343.15	0.5167
0.0840	343.15	0.6283
0.1183	343.15	0.6990
0.1950	343.15	0.7718
0.2363	343.15	0.7899
0.2841	343.15	0.8116
0.3271	343.15	0.8264
0.4620	343.15	0.8435
0.4950	343.15	0.8488
0.5641	343.15	0.8588
0.6250	343.15	0.8770
0.7353	343.15	0.8963
0.8350	343.15	0.9044
0.9254	343.15	0.9296
0.9545	343.15	0.9479
0.9782	343.15	0.9719
0.9969	343.15	0.9956
1.0000	343.15	1.0000

Mole fraction of n-Hexane (1) [ref]

Fixed		Measured
Mole fraction of n-Hexane (1) - Liquid	Temperature, K - Liquid	Mole fraction of n-Hexane (1) - Gas
0.0000	303.15	0.0000
0.0101	303.15	0.3570
0.0522	303.15	0.7149
0.0821	303.15	0.8046
0.1202	303.15	0.8529
0.1930	303.15	0.8924
0.2382	303.15	0.9079
0.2823	303.15	0.9197
0.3252	303.15	0.9243
0.4142	303.15	0.9343
0.4804	303.15	0.9427
0.5423	303.15	0.9467
0.6131	303.15	0.9507
0.7373	303.15	0.9538
0.8331	303.15	0.9558
0.9273	303.15	0.9607
0.9527	303.15	0.9658
0.9802	303.15	0.9812
0.9951	303.15	0.9945
1.0000	303.15	1.0000
0.0000	323.15	0.0000
0.0091	323.15	0.2349
0.0491	323.15	0.6158
0.0831	323.15	0.7274
0.1193	323.15	0.7838
0.1940	323.15	0.8428
0.2373	323.15	0.8589
0.2832	323.15	0.8806
0.3261	323.15	0.8873
0.4152	323.15	0.9063
0.4795	323.15	0.9090
0.5432	323.15	0.9140
0.6141	323.15	0.9170
0.7363	323.15	0.9190
0.8341	323.15	0.9208
0.9263	323.15	0.9486
0.9536	323.15	0.9588
0.9792	323.15	0.9783
0.9960	323.15	0.9954
1.0000	323.15	1.0000
0.0000	343.15	0.0000
0.0070	343.15	0.1465
0.0500	343.15	0.5167
0.0840	343.15	0.6283
0.1183	343.15	0.6990
0.1950	343.15	0.7718
0.2363	343.15	0.7899
0.2841	343.15	0.8116
0.3271	343.15	0.8264
0.4620	343.15	0.8435
0.4950	343.15	0.8488
0.5641	343.15	0.8588
0.6250	343.15	0.8770
0.7353	343.15	0.8963
0.8350	343.15	0.9044
0.9254	343.15	0.9296
0.9545	343.15	0.9479
0.9782	343.15	0.9719
0.9969	343.15	0.9956
1.0000	343.15	1.0000

Viscosity, Pa*s [ref]

Operational conditions:

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

Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.0003
0.0554	0.0003
0.1040	0.0003
0.2000	0.0004
0.3274	0.0005
0.4173	0.0005
0.4666	0.0006
0.5057	0.0007
0.5589	0.0007
0.6090	0.0009
0.7073	0.0012
0.8051	0.0016
0.8610	0.0020
0.9149	0.0025
0.9376	0.0027
1.0000	0.0034

Viscosity, Pa*s [ref]

Operational conditions:

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

Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Viscosity, Pa*s - Liquid
0.0000	0.0003
0.0554	0.0003
0.1040	0.0003
0.2000	0.0004
0.3274	0.0005
0.4173	0.0005
0.4666	0.0006
0.5057	0.0007
0.5589	0.0007
0.6090	0.0009
0.7073	0.0012
0.8051	0.0016
0.8610	0.0020
0.9149	0.0025
0.9376	0.0027
1.0000	0.0034

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of n-Hexane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	303.15	2.01
0.0101	303.15	2.99
0.0522	303.15	6.81
0.0821	303.15	9.48
0.1202	303.15	11.85
0.1930	303.15	15.72
0.2382	303.15	17.37
0.2823	303.15	18.71
0.3252	303.15	20.07
0.4142	303.15	21.72
0.4804	303.15	22.34
0.5423	303.15	22.75
0.6131	303.15	23.28
0.7373	303.15	23.81
0.8331	303.15	24.09
0.9273	303.15	24.72
0.9527	303.15	24.81
0.9802	303.15	24.89
0.9951	303.15	25.01
1.0000	303.15	25.09
0.0000	323.15	7.11
0.0091	323.15	8.94
0.0491	323.15	17.96
0.0831	323.15	23.50
0.1193	323.15	29.21
0.1940	323.15	37.81
0.2373	323.15	41.92
0.2832	323.15	46.40
0.3261	323.15	48.69
0.4152	323.15	52.03
0.4795	323.15	53.36
0.5432	323.15	54.37
0.6141	323.15	54.50
0.7363	323.15	54.60
0.8341	323.15	54.84
0.9263	323.15	55.48
0.9536	323.15	55.52
0.9792	323.15	55.72
0.9960	323.15	55.02
1.0000	323.15	54.30
0.0000	343.15	20.47
0.0070	343.15	23.87
0.0500	343.15	40.92
0.0840	343.15	51.79
0.1183	343.15	61.21
0.1950	343.15	75.63
0.2363	343.15	80.73
0.2841	343.15	86.03
0.3271	343.15	91.08
0.4620	343.15	99.50
0.4950	343.15	102.46
0.5641	343.15	105.05
0.6250	343.15	106.60
0.7353	343.15	107.90
0.8350	343.15	108.80
0.9254	343.15	108.96
0.9545	343.15	109.05
0.9782	343.15	108.43
0.9969	343.15	107.05
1.0000	343.15	105.38

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of n-Hexane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	303.15	2.01
0.0101	303.15	2.99
0.0522	303.15	6.81
0.0821	303.15	9.48
0.1202	303.15	11.85
0.1930	303.15	15.72
0.2382	303.15	17.37
0.2823	303.15	18.71
0.3252	303.15	20.07
0.4142	303.15	21.72
0.4804	303.15	22.34
0.5423	303.15	22.75
0.6131	303.15	23.28
0.7373	303.15	23.81
0.8331	303.15	24.09
0.9273	303.15	24.72
0.9527	303.15	24.81
0.9802	303.15	24.89
0.9951	303.15	25.01
1.0000	303.15	25.09
0.0000	323.15	7.11
0.0091	323.15	8.94
0.0491	323.15	17.96
0.0831	323.15	23.50
0.1193	323.15	29.21
0.1940	323.15	37.81
0.2373	323.15	41.92
0.2832	323.15	46.40
0.3261	323.15	48.69
0.4152	323.15	52.03
0.4795	323.15	53.36
0.5432	323.15	54.37
0.6141	323.15	54.50
0.7363	323.15	54.60
0.8341	323.15	54.84
0.9263	323.15	55.48
0.9536	323.15	55.52
0.9792	323.15	55.72
0.9960	323.15	55.02
1.0000	323.15	54.30
0.0000	343.15	20.47
0.0070	343.15	23.87
0.0500	343.15	40.92
0.0840	343.15	51.79
0.1183	343.15	61.21
0.1950	343.15	75.63
0.2363	343.15	80.73
0.2841	343.15	86.03
0.3271	343.15	91.08
0.4620	343.15	99.50
0.4950	343.15	102.46
0.5641	343.15	105.05
0.6250	343.15	106.60
0.7353	343.15	107.90
0.8350	343.15	108.80
0.9254	343.15	108.96
0.9545	343.15	109.05
0.9782	343.15	108.43
0.9969	343.15	107.05
1.0000	343.15	105.38

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	654.9
0.0554	660.1
0.1040	664.9
0.2000	675.1
0.3274	690.1
0.4173	701.6
0.4666	708.3
0.5057	713.8
0.5589	721.5
0.6090	729.0
0.7073	744.6
0.8051	761.2
0.8610	771.2
0.9149	781.3
0.9376	785.7
1.0000	798.2

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	654.9
0.0554	660.1
0.1040	664.9
0.2000	675.1
0.3274	690.1
0.4173	701.6
0.4666	708.3
0.5057	713.8
0.5589	721.5
0.6090	729.0
0.7073	744.6
0.8051	761.2
0.8610	771.2
0.9149	781.3
0.9376	785.7
1.0000	798.2

Speed of sound, m/s [ref]

Operational conditions:

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

Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1078.5
0.0554	1077.54
0.1040	1077.48
0.2000	1080.12
0.3274	1086.69
0.4173	1094.14
0.4666	1099.2
0.5057	1103.48
0.5589	1110.04
0.6090	1116.92
0.7073	1132.47
0.8051	1150.02
0.8610	1161.26
0.9149	1172.51
0.9376	1177.52
1.0000	1191.35

Speed of sound, m/s [ref]

Operational conditions:

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

Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1078.5
0.0554	1077.54
0.1040	1077.48
0.2000	1080.12
0.3274	1086.69
0.4173	1094.14
0.4666	1099.2
0.5057	1103.48
0.5589	1110.04
0.6090	1116.92
0.7073	1132.47
0.8051	1150.02
0.8610	1161.26
0.9149	1172.51
0.9376	1177.52
1.0000	1191.35

Sources

• Isothermal Vapor-Liquid Equilibrium Measurements for Alcohol + Water/n-Hexane Azeotropic Systems Using Both Dynamic and Automated Static-Synthetic Methods
• Thermophysical Properties of Binary Mixtures of 2-Methyl-1-propanol with Hexane, Octane, and Decane at 298.15 K