Mixture of 2-Butanone + 1-Pentanol

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (2)
3. P_vap - Vapor or sublimation pressure, kPa (2)
4. n₀ - Refractive index (Na D-line) (2)
5. ρ_l - Mass density, kg/m3 (2)

Mole fraction of 2-Butanone (1) [ref]

Fixed		Measured
Mole fraction of 2-Butanone (1) - Liquid	Temperature, K - Liquid	Mole fraction of 2-Butanone (1) - Gas
0.0000	333.65	0.0000
0.0050	333.65	0.1150
0.0090	333.65	0.1850
0.0170	333.65	0.2900
0.0320	333.65	0.4410
0.0650	333.65	0.6180
0.1290	333.65	0.7680
0.2190	333.65	0.8670
0.3400	333.65	0.9110
0.4190	333.65	0.9310
0.5210	333.65	0.9430
0.6310	333.65	0.9610
0.6920	333.65	0.9680
0.7500	333.65	0.9710
0.8390	333.65	0.9810
0.9000	333.65	0.9850
0.9400	333.65	0.9900
0.9590	333.65	0.9930
0.9800	333.65	0.9970
0.9900	333.65	0.9980
0.9980	333.65	0.9990
1.0000	333.65	1.0000
0.0000	343.55	0.0000
0.0040	343.55	0.0810
0.0080	343.55	0.1450
0.0170	343.55	0.2550
0.0350	343.55	0.4190
0.0620	343.55	0.5590
0.1240	343.55	0.7300
0.2290	343.55	0.8370
0.3700	343.55	0.8990
0.4520	343.55	0.9210
0.5220	343.55	0.9340
0.5740	343.55	0.9420
0.6500	343.55	0.9530
0.7890	343.55	0.9710
0.9240	343.55	0.9890
0.9480	343.55	0.9900
0.9800	343.55	0.9950
0.9900	343.55	0.9970
0.9950	343.55	0.9980
1.0000	343.55	1.0000
0.0000	348.55	0.0000
0.0050	348.55	0.0880
0.0080	348.55	0.1320
0.0170	348.55	0.2350
0.0340	348.55	0.3840
0.0590	348.55	0.5260
0.1250	348.55	0.7100
0.2280	348.55	0.8220
0.3570	348.55	0.8870
0.4390	348.55	0.9120
0.5130	348.55	0.9260
0.5500	348.55	0.9330
0.6140	348.55	0.9520
0.7390	348.55	0.9630
0.9340	348.55	0.9860
0.9540	348.55	0.9900
0.9730	348.55	0.9940
0.9860	348.55	0.9970
0.9920	348.55	0.9970
0.9960	348.55	0.9980
0.9990	348.55	1.0000
1.0000	348.55	1.0000

Mole fraction of 2-Butanone (1) [ref]

Fixed		Measured
Mole fraction of 2-Butanone (1) - Liquid	Temperature, K - Liquid	Mole fraction of 2-Butanone (1) - Gas
0.0000	333.65	0.0000
0.0050	333.65	0.1150
0.0090	333.65	0.1850
0.0170	333.65	0.2900
0.0320	333.65	0.4410
0.0650	333.65	0.6180
0.1290	333.65	0.7680
0.2190	333.65	0.8670
0.3400	333.65	0.9110
0.4190	333.65	0.9310
0.5210	333.65	0.9430
0.6310	333.65	0.9610
0.6920	333.65	0.9680
0.7500	333.65	0.9710
0.8390	333.65	0.9810
0.9000	333.65	0.9850
0.9400	333.65	0.9900
0.9590	333.65	0.9930
0.9800	333.65	0.9970
0.9900	333.65	0.9980
0.9980	333.65	0.9990
1.0000	333.65	1.0000
0.0000	343.55	0.0000
0.0040	343.55	0.0810
0.0080	343.55	0.1450
0.0170	343.55	0.2550
0.0350	343.55	0.4190
0.0620	343.55	0.5590
0.1240	343.55	0.7300
0.2290	343.55	0.8370
0.3700	343.55	0.8990
0.4520	343.55	0.9210
0.5220	343.55	0.9340
0.5740	343.55	0.9420
0.6500	343.55	0.9530
0.7890	343.55	0.9710
0.9240	343.55	0.9890
0.9480	343.55	0.9900
0.9800	343.55	0.9950
0.9900	343.55	0.9970
0.9950	343.55	0.9980
1.0000	343.55	1.0000
0.0000	348.55	0.0000
0.0050	348.55	0.0880
0.0080	348.55	0.1320
0.0170	348.55	0.2350
0.0340	348.55	0.3840
0.0590	348.55	0.5260
0.1250	348.55	0.7100
0.2280	348.55	0.8220
0.3570	348.55	0.8870
0.4390	348.55	0.9120
0.5130	348.55	0.9260
0.5500	348.55	0.9330
0.6140	348.55	0.9520
0.7390	348.55	0.9630
0.9340	348.55	0.9860
0.9540	348.55	0.9900
0.9730	348.55	0.9940
0.9860	348.55	0.9970
0.9920	348.55	0.9970
0.9960	348.55	0.9980
0.9990	348.55	1.0000
1.0000	348.55	1.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanone (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0035
298.15	0.0880	0.0026
298.15	0.1632	0.0020
298.15	0.2427	0.0016
298.15	0.3549	0.0012
298.15	0.4434	0.0010
298.15	0.5597	0.0008
298.15	0.6518	0.0006
298.15	0.7401	0.0006
298.15	0.8477	0.0005
298.15	0.9355	0.0004
298.15	1.0000	0.0004
308.15	0.0000	0.0027
308.15	0.0880	0.0020
308.15	0.1632	0.0016
308.15	0.2427	0.0013
308.15	0.3549	0.0010
308.15	0.4434	0.0008
308.15	0.5597	0.0007
308.15	0.6518	0.0006
308.15	0.7401	0.0005
308.15	0.8477	0.0004
308.15	0.9355	0.0004
308.15	1.0000	0.0004
318.15	0.0000	0.0023
318.15	0.0880	0.0016
318.15	0.1632	0.0013
318.15	0.2427	0.0011
318.15	0.3549	0.0009
318.15	0.4434	0.0007
318.15	0.5597	0.0006
318.15	0.6518	0.0005
318.15	0.7401	0.0004
318.15	0.8477	0.0004
318.15	0.9355	0.0003
318.15	1.0000	0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanone (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0035
298.15	0.0880	0.0026
298.15	0.1632	0.0020
298.15	0.2427	0.0016
298.15	0.3549	0.0012
298.15	0.4434	0.0010
298.15	0.5597	0.0008
298.15	0.6518	0.0006
298.15	0.7401	0.0006
298.15	0.8477	0.0005
298.15	0.9355	0.0004
298.15	1.0000	0.0004
308.15	0.0000	0.0027
308.15	0.0880	0.0020
308.15	0.1632	0.0016
308.15	0.2427	0.0013
308.15	0.3549	0.0010
308.15	0.4434	0.0008
308.15	0.5597	0.0007
308.15	0.6518	0.0006
308.15	0.7401	0.0005
308.15	0.8477	0.0004
308.15	0.9355	0.0004
308.15	1.0000	0.0004
318.15	0.0000	0.0023
318.15	0.0880	0.0016
318.15	0.1632	0.0013
318.15	0.2427	0.0011
318.15	0.3549	0.0009
318.15	0.4434	0.0007
318.15	0.5597	0.0006
318.15	0.6518	0.0005
318.15	0.7401	0.0004
318.15	0.8477	0.0004
318.15	0.9355	0.0003
318.15	1.0000	0.0003

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 2-Butanone (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	333.65	3.43
0.0050	333.65	3.87
0.0090	333.65	4.20
0.0170	333.65	4.80
0.0320	333.65	6.00
0.0650	333.65	8.52
0.1290	333.65	13.15
0.2190	333.65	20.40
0.3400	333.65	26.60
0.4190	333.65	31.30
0.5210	333.65	34.70
0.6310	333.65	38.81
0.6920	333.65	40.67
0.7500	333.65	42.12
0.8390	333.65	45.60
0.9000	333.65	48.16
0.9400	333.65	49.85
0.9590	333.65	50.65
0.9800	333.65	51.60
0.9900	333.65	52.02
0.9980	333.65	52.37
1.0000	333.65	52.42
0.0000	343.55	5.90
0.0040	343.55	6.50
0.0080	343.55	6.86
0.0170	343.55	7.98
0.0350	343.55	9.88
0.0620	343.55	12.95
0.1240	343.55	19.13
0.2290	343.55	28.30
0.3700	343.55	38.29
0.4520	343.55	43.63
0.5220	343.55	47.44
0.5740	343.55	50.68
0.6500	343.55	54.73
0.7890	343.55	61.91
0.9240	343.55	70.50
0.9480	343.55	71.91
0.9800	343.55	73.89
0.9900	343.55	74.40
0.9950	343.55	74.65
1.0000	343.55	74.79
0.0000	348.55	7.67
0.0050	348.55	8.42
0.0080	348.55	8.90
0.0170	348.55	10.04
0.0340	348.55	12.25
0.0590	348.55	15.15
0.1250	348.55	23.59
0.2280	348.55	33.95
0.3570	348.55	44.93
0.4390	348.55	50.61
0.5130	348.55	54.10
0.5500	348.55	57.21
0.6140	348.55	62.21
0.7390	348.55	70.25
0.9340	348.55	84.70
0.9540	348.55	85.52
0.9730	348.55	86.89
0.9860	348.55	87.60
0.9920	348.55	87.95
0.9960	348.55	88.12
0.9990	348.55	88.25
1.0000	348.55	88.29

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 2-Butanone (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	333.65	3.43
0.0050	333.65	3.87
0.0090	333.65	4.20
0.0170	333.65	4.80
0.0320	333.65	6.00
0.0650	333.65	8.52
0.1290	333.65	13.15
0.2190	333.65	20.40
0.3400	333.65	26.60
0.4190	333.65	31.30
0.5210	333.65	34.70
0.6310	333.65	38.81
0.6920	333.65	40.67
0.7500	333.65	42.12
0.8390	333.65	45.60
0.9000	333.65	48.16
0.9400	333.65	49.85
0.9590	333.65	50.65
0.9800	333.65	51.60
0.9900	333.65	52.02
0.9980	333.65	52.37
1.0000	333.65	52.42
0.0000	343.55	5.90
0.0040	343.55	6.50
0.0080	343.55	6.86
0.0170	343.55	7.98
0.0350	343.55	9.88
0.0620	343.55	12.95
0.1240	343.55	19.13
0.2290	343.55	28.30
0.3700	343.55	38.29
0.4520	343.55	43.63
0.5220	343.55	47.44
0.5740	343.55	50.68
0.6500	343.55	54.73
0.7890	343.55	61.91
0.9240	343.55	70.50
0.9480	343.55	71.91
0.9800	343.55	73.89
0.9900	343.55	74.40
0.9950	343.55	74.65
1.0000	343.55	74.79
0.0000	348.55	7.67
0.0050	348.55	8.42
0.0080	348.55	8.90
0.0170	348.55	10.04
0.0340	348.55	12.25
0.0590	348.55	15.15
0.1250	348.55	23.59
0.2280	348.55	33.95
0.3570	348.55	44.93
0.4390	348.55	50.61
0.5130	348.55	54.10
0.5500	348.55	57.21
0.6140	348.55	62.21
0.7390	348.55	70.25
0.9340	348.55	84.70
0.9540	348.55	85.52
0.9730	348.55	86.89
0.9860	348.55	87.60
0.9920	348.55	87.95
0.9960	348.55	88.12
0.9990	348.55	88.25
1.0000	348.55	88.29

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanone (1) - Liquid	Refractive index (Na D-line) - Liquid
298.15	0.0000	1.4068
298.15	0.0880	1.4049
298.15	0.1632	1.4031
298.15	0.2427	1.401
298.15	0.3549	1.3979
298.15	0.4434	1.3953
298.15	0.5597	1.3915
298.15	0.6518	1.3883
298.15	0.7401	1.3851
298.15	0.8477	1.381
298.15	0.9355	1.3776
298.15	1.0000	1.375
308.15	0.0000	1.4031
308.15	0.0880	1.4014
308.15	0.1632	1.3997
308.15	0.2427	1.3976
308.15	0.3549	1.3943
308.15	0.4434	1.3914
308.15	0.5597	1.3873
308.15	0.6518	1.3838
308.15	0.7401	1.3804
308.15	0.8477	1.376
308.15	0.9355	1.3725
308.15	1.0000	1.37
318.15	0.0000	1.3996
318.15	0.0880	1.3976
318.15	0.1632	1.3957
318.15	0.2427	1.3937
318.15	0.3549	1.3905
318.15	0.4434	1.3878
318.15	0.5597	1.3838
318.15	0.6518	1.3804
318.15	0.7401	1.377
318.15	0.8477	1.3724
318.15	0.9355	1.3686
318.15	1.0000	1.3657

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanone (1) - Liquid	Refractive index (Na D-line) - Liquid
298.15	0.0000	1.4068
298.15	0.0880	1.4049
298.15	0.1632	1.4031
298.15	0.2427	1.401
298.15	0.3549	1.3979
298.15	0.4434	1.3953
298.15	0.5597	1.3915
298.15	0.6518	1.3883
298.15	0.7401	1.3851
298.15	0.8477	1.381
298.15	0.9355	1.3776
298.15	1.0000	1.375
308.15	0.0000	1.4031
308.15	0.0880	1.4014
308.15	0.1632	1.3997
308.15	0.2427	1.3976
308.15	0.3549	1.3943
308.15	0.4434	1.3914
308.15	0.5597	1.3873
308.15	0.6518	1.3838
308.15	0.7401	1.3804
308.15	0.8477	1.376
308.15	0.9355	1.3725
308.15	1.0000	1.37
318.15	0.0000	1.3996
318.15	0.0880	1.3976
318.15	0.1632	1.3957
318.15	0.2427	1.3937
318.15	0.3549	1.3905
318.15	0.4434	1.3878
318.15	0.5597	1.3838
318.15	0.6518	1.3804
318.15	0.7401	1.377
318.15	0.8477	1.3724
318.15	0.9355	1.3686
318.15	1.0000	1.3657

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanone (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	810.85
298.15	0.0880	809.94
298.15	0.1632	809.15
298.15	0.2427	808.31
298.15	0.3549	807.11
298.15	0.4434	806.15
298.15	0.5597	804.87
298.15	0.6518	803.85
298.15	0.7401	802.85
298.15	0.8477	801.59
298.15	0.9355	800.55
298.15	1.0000	799.76
308.15	0.0000	803.45
308.15	0.0880	802.26
308.15	0.1632	801.25
308.15	0.2427	800.16
308.15	0.3549	798.62
308.15	0.4434	797.39
308.15	0.5597	795.76
308.15	0.6518	794.44
308.15	0.7401	793.14
308.15	0.8477	791.54
308.15	0.9355	790.21
308.15	1.0000	789.21
318.15	0.0000	795.9
318.15	0.0880	794.44
318.15	0.1632	793.21
318.15	0.2427	791.89
318.15	0.3549	789.99
318.15	0.4434	788.5
318.15	0.5597	786.5
318.15	0.6518	784.88
318.15	0.7401	783.31
318.15	0.8477	781.36
318.15	0.9355	779.73
318.15	1.0000	778.52

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Butanone (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	810.85
298.15	0.0880	809.94
298.15	0.1632	809.15
298.15	0.2427	808.31
298.15	0.3549	807.11
298.15	0.4434	806.15
298.15	0.5597	804.87
298.15	0.6518	803.85
298.15	0.7401	802.85
298.15	0.8477	801.59
298.15	0.9355	800.55
298.15	1.0000	799.76
308.15	0.0000	803.45
308.15	0.0880	802.26
308.15	0.1632	801.25
308.15	0.2427	800.16
308.15	0.3549	798.62
308.15	0.4434	797.39
308.15	0.5597	795.76
308.15	0.6518	794.44
308.15	0.7401	793.14
308.15	0.8477	791.54
308.15	0.9355	790.21
308.15	1.0000	789.21
318.15	0.0000	795.9
318.15	0.0880	794.44
318.15	0.1632	793.21
318.15	0.2427	791.89
318.15	0.3549	789.99
318.15	0.4434	788.5
318.15	0.5597	786.5
318.15	0.6518	784.88
318.15	0.7401	783.31
318.15	0.8477	781.36
318.15	0.9355	779.73
318.15	1.0000	778.52

Sources

• Isothermal Vapor-Liquid Equilibrium Measurements of Butan-2-one + 2-Methyl-propan-1-ol/Pentan-1-ol
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures