Mixture of 2-Butanone + 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)

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	332.65	0.0000
0.0100	332.65	0.1270
0.0280	332.65	0.2460
0.0400	332.65	0.2860
0.0500	332.65	0.3150
0.1170	332.65	0.4910
0.1620	332.65	0.5690
0.2370	332.65	0.6500
0.3000	332.65	0.7080
0.4690	332.65	0.7890
0.6440	332.65	0.8630
0.7100	332.65	0.8870
0.8460	332.65	0.9360
0.9080	332.65	0.9620
0.9470	332.65	0.9750
0.9700	332.65	0.9850
0.9800	332.65	0.9890
1.0000	332.65	1.0000
0.0000	342.63	0.0000
0.0110	342.63	0.1010
0.0290	342.63	0.1900
0.0410	342.63	0.2350
0.0500	342.63	0.2600
0.1180	342.63	0.4400
0.1690	342.63	0.5350
0.2350	342.63	0.6080
0.2960	342.63	0.6630
0.4730	342.63	0.7720
0.6510	342.63	0.8500
0.6940	342.63	0.8690
0.8460	342.63	0.9280
0.9260	342.63	0.9560
0.9360	342.63	0.9610
0.9750	342.63	0.9840
0.9830	342.63	0.9890
1.0000	342.63	1.0000
0.0000	349.06	0.0000
0.0110	349.06	0.0660
0.0200	349.06	0.1060
0.0240	349.06	0.1220
0.0250	349.06	0.1280
0.0520	349.06	0.2240
0.0850	349.06	0.3200
0.1190	349.06	0.3950
0.2510	349.06	0.5860
0.3200	349.06	0.6480
0.4780	349.06	0.7550
0.6940	349.06	0.8580
0.8650	349.06	0.9290
0.9170	349.06	0.9480
0.9310	349.06	0.9550
0.9820	349.06	0.9870
0.9910	349.06	0.9930
1.0000	349.06	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	332.65	0.0000
0.0100	332.65	0.1270
0.0280	332.65	0.2460
0.0400	332.65	0.2860
0.0500	332.65	0.3150
0.1170	332.65	0.4910
0.1620	332.65	0.5690
0.2370	332.65	0.6500
0.3000	332.65	0.7080
0.4690	332.65	0.7890
0.6440	332.65	0.8630
0.7100	332.65	0.8870
0.8460	332.65	0.9360
0.9080	332.65	0.9620
0.9470	332.65	0.9750
0.9700	332.65	0.9850
0.9800	332.65	0.9890
1.0000	332.65	1.0000
0.0000	342.63	0.0000
0.0110	342.63	0.1010
0.0290	342.63	0.1900
0.0410	342.63	0.2350
0.0500	342.63	0.2600
0.1180	342.63	0.4400
0.1690	342.63	0.5350
0.2350	342.63	0.6080
0.2960	342.63	0.6630
0.4730	342.63	0.7720
0.6510	342.63	0.8500
0.6940	342.63	0.8690
0.8460	342.63	0.9280
0.9260	342.63	0.9560
0.9360	342.63	0.9610
0.9750	342.63	0.9840
0.9830	342.63	0.9890
1.0000	342.63	1.0000
0.0000	349.06	0.0000
0.0110	349.06	0.0660
0.0200	349.06	0.1060
0.0240	349.06	0.1220
0.0250	349.06	0.1280
0.0520	349.06	0.2240
0.0850	349.06	0.3200
0.1190	349.06	0.3950
0.2510	349.06	0.5860
0.3200	349.06	0.6480
0.4780	349.06	0.7550
0.6940	349.06	0.8580
0.8650	349.06	0.9290
0.9170	349.06	0.9480
0.9310	349.06	0.9550
0.9820	349.06	0.9870
0.9910	349.06	0.9930
1.0000	349.06	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
293.15	0.0000	0.0040
293.15	0.0684	0.0031
293.15	0.1365	0.0024
293.15	0.2044	0.0019
293.15	0.2721	0.0014
293.15	0.3395	0.0011
293.15	0.4066	0.0009
293.15	0.4735	0.0007
293.15	0.5402	0.0006
293.15	0.6066	0.0005
293.15	0.6727	0.0005
293.15	0.7387	0.0005
293.15	0.8044	0.0005
293.15	0.8698	0.0005
293.15	0.9350	0.0005
293.15	1.0000	0.0004
298.15	0.0000	0.0033
298.15	0.0684	0.0026
298.15	0.1365	0.0021
298.15	0.2044	0.0016
298.15	0.2721	0.0012
298.15	0.3395	0.0009
298.15	0.4066	0.0008
298.15	0.4735	0.0006
298.15	0.5402	0.0005
298.15	0.6066	0.0005
298.15	0.6727	0.0005
298.15	0.7387	0.0004
298.15	0.8044	0.0004
298.15	0.8698	0.0004
298.15	0.9350	0.0004
298.15	1.0000	0.0003
303.15	0.0000	0.0029
303.15	0.0684	0.0022
303.15	0.1365	0.0018
303.15	0.2044	0.0014
303.15	0.2721	0.0011
303.15	0.3395	0.0009
303.15	0.4066	0.0007
303.15	0.4735	0.0005
303.15	0.5402	0.0005
303.15	0.6066	0.0004
303.15	0.6727	0.0004
303.15	0.7387	0.0004
303.15	0.8044	0.0004
303.15	0.8698	0.0003
303.15	0.9350	0.0003
303.15	1.0000	0.0003
308.15	0.0000	0.0024
308.15	0.0684	0.0019
308.15	0.1365	0.0015
308.15	0.2044	0.0012
308.15	0.2721	0.0010
308.15	0.3395	0.0008
308.15	0.4066	0.0006
308.15	0.4735	0.0005
308.15	0.5402	0.0004
308.15	0.6066	0.0004
308.15	0.6727	0.0004
308.15	0.7387	0.0004
308.15	0.8044	0.0003
308.15	0.8698	0.0003
308.15	0.9350	0.0003
308.15	1.0000	0.0003
313.15	0.0000	0.0020
313.15	0.0684	0.0016
313.15	0.1365	0.0013
313.15	0.2044	0.0011
313.15	0.2721	0.0009
313.15	0.3395	0.0007
313.15	0.4066	0.0006
313.15	0.4735	0.0005
313.15	0.5402	0.0004
313.15	0.6066	0.0003
313.15	0.6727	0.0003
313.15	0.7387	0.0003
313.15	0.8044	0.0003
313.15	0.8698	0.0003
313.15	0.9350	0.0003
313.15	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
293.15	0.0000	0.0040
293.15	0.0684	0.0031
293.15	0.1365	0.0024
293.15	0.2044	0.0019
293.15	0.2721	0.0014
293.15	0.3395	0.0011
293.15	0.4066	0.0009
293.15	0.4735	0.0007
293.15	0.5402	0.0006
293.15	0.6066	0.0005
293.15	0.6727	0.0005
293.15	0.7387	0.0005
293.15	0.8044	0.0005
293.15	0.8698	0.0005
293.15	0.9350	0.0005
293.15	1.0000	0.0004
298.15	0.0000	0.0033
298.15	0.0684	0.0026
298.15	0.1365	0.0021
298.15	0.2044	0.0016
298.15	0.2721	0.0012
298.15	0.3395	0.0009
298.15	0.4066	0.0008
298.15	0.4735	0.0006
298.15	0.5402	0.0005
298.15	0.6066	0.0005
298.15	0.6727	0.0005
298.15	0.7387	0.0004
298.15	0.8044	0.0004
298.15	0.8698	0.0004
298.15	0.9350	0.0004
298.15	1.0000	0.0003
303.15	0.0000	0.0029
303.15	0.0684	0.0022
303.15	0.1365	0.0018
303.15	0.2044	0.0014
303.15	0.2721	0.0011
303.15	0.3395	0.0009
303.15	0.4066	0.0007
303.15	0.4735	0.0005
303.15	0.5402	0.0005
303.15	0.6066	0.0004
303.15	0.6727	0.0004
303.15	0.7387	0.0004
303.15	0.8044	0.0004
303.15	0.8698	0.0003
303.15	0.9350	0.0003
303.15	1.0000	0.0003
308.15	0.0000	0.0024
308.15	0.0684	0.0019
308.15	0.1365	0.0015
308.15	0.2044	0.0012
308.15	0.2721	0.0010
308.15	0.3395	0.0008
308.15	0.4066	0.0006
308.15	0.4735	0.0005
308.15	0.5402	0.0004
308.15	0.6066	0.0004
308.15	0.6727	0.0004
308.15	0.7387	0.0004
308.15	0.8044	0.0003
308.15	0.8698	0.0003
308.15	0.9350	0.0003
308.15	1.0000	0.0003
313.15	0.0000	0.0020
313.15	0.0684	0.0016
313.15	0.1365	0.0013
313.15	0.2044	0.0011
313.15	0.2721	0.0009
313.15	0.3395	0.0007
313.15	0.4066	0.0006
313.15	0.4735	0.0005
313.15	0.5402	0.0004
313.15	0.6066	0.0003
313.15	0.6727	0.0003
313.15	0.7387	0.0003
313.15	0.8044	0.0003
313.15	0.8698	0.0003
313.15	0.9350	0.0003
313.15	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	332.65	12.17
0.0100	332.65	13.80
0.0280	332.65	15.70
0.0400	332.65	16.40
0.0500	332.65	17.02
0.1170	332.65	21.35
0.1620	332.65	24.24
0.2370	332.65	28.03
0.3000	332.65	30.82
0.4690	332.65	36.31
0.6440	332.65	41.79
0.7100	332.65	43.69
0.8460	332.65	47.77
0.9080	332.65	49.47
0.9470	332.65	50.57
0.9700	332.65	51.01
0.9800	332.65	51.40
1.0000	332.65	51.76
0.0000	342.63	20.07
0.0110	342.63	22.20
0.0290	342.63	24.10
0.0410	342.63	25.30
0.0500	342.63	26.20
0.1180	342.63	33.12
0.1690	342.63	37.51
0.2350	342.63	41.39
0.2960	342.63	45.28
0.4730	342.63	52.86
0.6510	342.63	61.54
0.6940	342.63	63.23
0.8460	342.63	68.32
0.9260	342.63	70.60
0.9360	342.63	70.91
0.9750	342.63	72.10
0.9830	342.63	72.49
1.0000	342.63	72.71
0.0000	349.06	26.53
0.0110	349.06	28.70
0.0200	349.06	29.95
0.0240	349.06	30.00
0.0250	349.06	30.10
0.0520	349.06	33.15
0.0850	349.06	37.10
0.1190	349.06	40.50
0.2510	349.06	49.77
0.3200	349.06	54.51
0.4780	349.06	64.03
0.6940	349.06	74.80
0.8650	349.06	85.08
0.9170	349.06	87.28
0.9310	349.06	87.91
0.9820	349.06	89.80
0.9910	349.06	89.93
1.0000	349.06	90.10

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	332.65	12.17
0.0100	332.65	13.80
0.0280	332.65	15.70
0.0400	332.65	16.40
0.0500	332.65	17.02
0.1170	332.65	21.35
0.1620	332.65	24.24
0.2370	332.65	28.03
0.3000	332.65	30.82
0.4690	332.65	36.31
0.6440	332.65	41.79
0.7100	332.65	43.69
0.8460	332.65	47.77
0.9080	332.65	49.47
0.9470	332.65	50.57
0.9700	332.65	51.01
0.9800	332.65	51.40
1.0000	332.65	51.76
0.0000	342.63	20.07
0.0110	342.63	22.20
0.0290	342.63	24.10
0.0410	342.63	25.30
0.0500	342.63	26.20
0.1180	342.63	33.12
0.1690	342.63	37.51
0.2350	342.63	41.39
0.2960	342.63	45.28
0.4730	342.63	52.86
0.6510	342.63	61.54
0.6940	342.63	63.23
0.8460	342.63	68.32
0.9260	342.63	70.60
0.9360	342.63	70.91
0.9750	342.63	72.10
0.9830	342.63	72.49
1.0000	342.63	72.71
0.0000	349.06	26.53
0.0110	349.06	28.70
0.0200	349.06	29.95
0.0240	349.06	30.00
0.0250	349.06	30.10
0.0520	349.06	33.15
0.0850	349.06	37.10
0.1190	349.06	40.50
0.2510	349.06	49.77
0.3200	349.06	54.51
0.4780	349.06	64.03
0.6940	349.06	74.80
0.8650	349.06	85.08
0.9170	349.06	87.28
0.9310	349.06	87.91
0.9820	349.06	89.80
0.9910	349.06	89.93
1.0000	349.06	90.10

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
293.15	0.0000	801.68
293.15	0.0684	801.9
293.15	0.1365	802.11
293.15	0.2044	802.32
293.15	0.2721	802.52
293.15	0.3395	802.72
293.15	0.4066	802.92
293.15	0.4735	803.13
293.15	0.5402	803.33
293.15	0.6066	803.54
293.15	0.6727	803.75
293.15	0.7387	803.97
293.15	0.8044	804.2
293.15	0.8698	804.43
293.15	0.9350	804.67
293.15	1.0000	804.92
298.15	0.0000	797.8
298.15	0.0684	797.93
298.15	0.1365	798.06
298.15	0.2044	798.18
298.15	0.2721	798.29
298.15	0.3395	798.41
298.15	0.4066	798.52
298.15	0.4735	798.63
298.15	0.5402	798.75
298.15	0.6066	798.87
298.15	0.6727	798.99
298.15	0.7387	799.12
298.15	0.8044	799.25
298.15	0.8698	799.4
298.15	0.9350	799.54
298.15	1.0000	799.7
303.15	0.0000	794.16
303.15	0.0684	794.21
303.15	0.1365	794.25
303.15	0.2044	794.29
303.15	0.2721	794.32
303.15	0.3395	794.36
303.15	0.4066	794.39
303.15	0.4735	794.42
303.15	0.5402	794.46
303.15	0.6066	794.49
303.15	0.6727	794.53
303.15	0.7387	794.58
303.15	0.8044	794.63
303.15	0.8698	794.68
303.15	0.9350	794.74
303.15	1.0000	794.81
308.15	0.0000	790.06
308.15	0.0684	790.04
308.15	0.1365	790.03
308.15	0.2044	790.0
308.15	0.2721	789.98
308.15	0.3395	789.95
308.15	0.4066	789.92
308.15	0.4735	789.89
308.15	0.5402	789.87
308.15	0.6066	789.85
308.15	0.6727	789.83
308.15	0.7387	789.82
308.15	0.8044	789.81
308.15	0.8698	789.8
308.15	0.9350	789.79
308.15	1.0000	789.78
313.15	0.0000	786.7
313.15	0.0684	786.54
313.15	0.1365	786.39
313.15	0.2044	786.22
313.15	0.2721	786.06
313.15	0.3395	785.89
313.15	0.4066	785.73
313.15	0.4735	785.56
313.15	0.5402	785.4
313.15	0.6066	785.23
313.15	0.6727	785.08
313.15	0.7387	784.92
313.15	0.8044	784.77
313.15	0.8698	784.62
313.15	0.9350	784.47
313.15	1.0000	784.32

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
293.15	0.0000	801.68
293.15	0.0684	801.9
293.15	0.1365	802.11
293.15	0.2044	802.32
293.15	0.2721	802.52
293.15	0.3395	802.72
293.15	0.4066	802.92
293.15	0.4735	803.13
293.15	0.5402	803.33
293.15	0.6066	803.54
293.15	0.6727	803.75
293.15	0.7387	803.97
293.15	0.8044	804.2
293.15	0.8698	804.43
293.15	0.9350	804.67
293.15	1.0000	804.92
298.15	0.0000	797.8
298.15	0.0684	797.93
298.15	0.1365	798.06
298.15	0.2044	798.18
298.15	0.2721	798.29
298.15	0.3395	798.41
298.15	0.4066	798.52
298.15	0.4735	798.63
298.15	0.5402	798.75
298.15	0.6066	798.87
298.15	0.6727	798.99
298.15	0.7387	799.12
298.15	0.8044	799.25
298.15	0.8698	799.4
298.15	0.9350	799.54
298.15	1.0000	799.7
303.15	0.0000	794.16
303.15	0.0684	794.21
303.15	0.1365	794.25
303.15	0.2044	794.29
303.15	0.2721	794.32
303.15	0.3395	794.36
303.15	0.4066	794.39
303.15	0.4735	794.42
303.15	0.5402	794.46
303.15	0.6066	794.49
303.15	0.6727	794.53
303.15	0.7387	794.58
303.15	0.8044	794.63
303.15	0.8698	794.68
303.15	0.9350	794.74
303.15	1.0000	794.81
308.15	0.0000	790.06
308.15	0.0684	790.04
308.15	0.1365	790.03
308.15	0.2044	790.0
308.15	0.2721	789.98
308.15	0.3395	789.95
308.15	0.4066	789.92
308.15	0.4735	789.89
308.15	0.5402	789.87
308.15	0.6066	789.85
308.15	0.6727	789.83
308.15	0.7387	789.82
308.15	0.8044	789.81
308.15	0.8698	789.8
308.15	0.9350	789.79
308.15	1.0000	789.78
313.15	0.0000	786.7
313.15	0.0684	786.54
313.15	0.1365	786.39
313.15	0.2044	786.22
313.15	0.2721	786.06
313.15	0.3395	785.89
313.15	0.4066	785.73
313.15	0.4735	785.56
313.15	0.5402	785.4
313.15	0.6066	785.23
313.15	0.6727	785.08
313.15	0.7387	784.92
313.15	0.8044	784.77
313.15	0.8698	784.62
313.15	0.9350	784.47
313.15	1.0000	784.32

Sources

• Isothermal Vapor-Liquid Equilibrium Measurements of Butan-2-one + 2-Methyl-propan-1-ol/Pentan-1-ol
• Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K