Mixture of Butanoic acid + 1-Propanol, 2-methyl-

Datasets

1. Mole fraction (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)

Mole fraction of 1-Propanol, 2-methyl- (2) [ref]

Fixed		Measured
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of 1-Propanol, 2-methyl- (2) - Gas
0.0000	333.15	0.0000
0.0816	333.15	0.3946
0.0932	333.15	0.4323
0.1259	333.15	0.5096
0.1659	333.15	0.6009
0.2118	333.15	0.6693
0.2651	333.15	0.7359
0.3211	333.15	0.7927
0.3812	333.15	0.8411
0.4758	333.15	0.8908
0.5195	333.15	0.9187
0.6472	333.15	0.9546
0.7185	333.15	0.9712
0.7699	333.15	0.9789
0.8788	333.15	0.9925
1.0000	333.15	1.0000
0.0000	353.15	0.0000
0.0705	353.15	0.3288
0.1424	353.15	0.5212
0.2107	353.15	0.6336
0.2423	353.15	0.6818
0.2813	353.15	0.7217
0.3461	353.15	0.7743
0.3930	353.15	0.8168
0.4305	353.15	0.8478
0.4903	353.15	0.8857
0.5524	353.15	0.9157
0.6107	353.15	0.9382
0.6616	353.15	0.9536
0.7278	353.15	0.9699
0.8256	353.15	0.9861
1.0000	353.15	1.0000
0.0000	373.15	0.0000
0.0567	373.15	0.2420
0.0948	373.15	0.3631
0.1600	373.15	0.5156
0.3251	373.15	0.7247
0.3860	373.15	0.7745
0.4520	373.15	0.8321
0.4883	373.15	0.8530
0.5309	373.15	0.8751
0.5788	373.15	0.9033
0.6257	373.15	0.9232
0.6756	373.15	0.9479
0.6969	373.15	0.9528
0.7518	373.15	0.9680
0.8118	373.15	0.9814
0.8612	373.15	0.9858
1.0000	373.15	1.0000

Mole fraction of 1-Propanol, 2-methyl- (2) [ref]

Fixed		Measured
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Temperature, K - Liquid	Mole fraction of 1-Propanol, 2-methyl- (2) - Gas
0.0000	333.15	0.0000
0.0816	333.15	0.3946
0.0932	333.15	0.4323
0.1259	333.15	0.5096
0.1659	333.15	0.6009
0.2118	333.15	0.6693
0.2651	333.15	0.7359
0.3211	333.15	0.7927
0.3812	333.15	0.8411
0.4758	333.15	0.8908
0.5195	333.15	0.9187
0.6472	333.15	0.9546
0.7185	333.15	0.9712
0.7699	333.15	0.9789
0.8788	333.15	0.9925
1.0000	333.15	1.0000
0.0000	353.15	0.0000
0.0705	353.15	0.3288
0.1424	353.15	0.5212
0.2107	353.15	0.6336
0.2423	353.15	0.6818
0.2813	353.15	0.7217
0.3461	353.15	0.7743
0.3930	353.15	0.8168
0.4305	353.15	0.8478
0.4903	353.15	0.8857
0.5524	353.15	0.9157
0.6107	353.15	0.9382
0.6616	353.15	0.9536
0.7278	353.15	0.9699
0.8256	353.15	0.9861
1.0000	353.15	1.0000
0.0000	373.15	0.0000
0.0567	373.15	0.2420
0.0948	373.15	0.3631
0.1600	373.15	0.5156
0.3251	373.15	0.7247
0.3860	373.15	0.7745
0.4520	373.15	0.8321
0.4883	373.15	0.8530
0.5309	373.15	0.8751
0.5788	373.15	0.9033
0.6257	373.15	0.9232
0.6756	373.15	0.9479
0.6969	373.15	0.9528
0.7518	373.15	0.9680
0.8118	373.15	0.9814
0.8612	373.15	0.9858
1.0000	373.15	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	333.15	1.29
0.0816	333.15	1.95
0.0932	333.15	2.10
0.1259	333.15	2.49
0.1659	333.15	2.83
0.2118	333.15	3.38
0.2651	333.15	4.03
0.3211	333.15	4.58
0.3812	333.15	5.34
0.4758	333.15	6.30
0.5195	333.15	6.93
0.6472	333.15	8.23
0.7185	333.15	9.04
0.7699	333.15	9.81
0.8788	333.15	11.02
1.0000	333.15	12.36
0.0000	353.15	3.86
0.0705	353.15	5.53
0.1424	353.15	7.56
0.2107	353.15	9.55
0.2423	353.15	10.44
0.2813	353.15	11.32
0.3461	353.15	13.06
0.3930	353.15	14.59
0.4305	353.15	15.77
0.4903	353.15	17.38
0.5524	353.15	19.32
0.6107	353.15	20.99
0.6616	353.15	23.14
0.7278	353.15	24.93
0.8256	353.15	27.76
1.0000	353.15	33.22
0.0000	373.15	9.94
0.0567	373.15	13.68
0.0948	373.15	15.47
0.1600	373.15	19.10
0.3251	373.15	29.31
0.3860	373.15	33.34
0.4520	373.15	38.27
0.4883	373.15	40.90
0.5309	373.15	43.58
0.5788	373.15	47.71
0.6257	373.15	50.52
0.6756	373.15	53.73
0.6969	373.15	55.28
0.7518	373.15	59.49
0.8118	373.15	63.33
0.8612	373.15	66.21
1.0000	373.15	76.32

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	333.15	1.29
0.0816	333.15	1.95
0.0932	333.15	2.10
0.1259	333.15	2.49
0.1659	333.15	2.83
0.2118	333.15	3.38
0.2651	333.15	4.03
0.3211	333.15	4.58
0.3812	333.15	5.34
0.4758	333.15	6.30
0.5195	333.15	6.93
0.6472	333.15	8.23
0.7185	333.15	9.04
0.7699	333.15	9.81
0.8788	333.15	11.02
1.0000	333.15	12.36
0.0000	353.15	3.86
0.0705	353.15	5.53
0.1424	353.15	7.56
0.2107	353.15	9.55
0.2423	353.15	10.44
0.2813	353.15	11.32
0.3461	353.15	13.06
0.3930	353.15	14.59
0.4305	353.15	15.77
0.4903	353.15	17.38
0.5524	353.15	19.32
0.6107	353.15	20.99
0.6616	353.15	23.14
0.7278	353.15	24.93
0.8256	353.15	27.76
1.0000	353.15	33.22
0.0000	373.15	9.94
0.0567	373.15	13.68
0.0948	373.15	15.47
0.1600	373.15	19.10
0.3251	373.15	29.31
0.3860	373.15	33.34
0.4520	373.15	38.27
0.4883	373.15	40.90
0.5309	373.15	43.58
0.5788	373.15	47.71
0.6257	373.15	50.52
0.6756	373.15	53.73
0.6969	373.15	55.28
0.7518	373.15	59.49
0.8118	373.15	63.33
0.8612	373.15	66.21
1.0000	373.15	76.32

Sources

• Vapour-liquid equilibrium of carboxylic acid alcohol binary systems:2-Propanol + butyric acid, 2-butanol + butyric acid and 2-methyl-1-propanol + butyric acid