Mixture of Isopropyl Alcohol + 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 (4)

Mole fraction of Isopropyl Alcohol (1) [ref]

Fixed		Measured
Mole fraction of Isopropyl Alcohol (1) - Liquid	Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Gas
0.0000	333.15	0.0000
0.0515	333.15	0.1695
0.1299	333.15	0.3521
0.1698	333.15	0.4235
0.2192	333.15	0.4992
0.2598	333.15	0.5499
0.3117	333.15	0.6073
0.3546	333.15	0.6470
0.3895	333.15	0.6773
0.4605	333.15	0.7319
0.5803	333.15	0.8061
0.7187	333.15	0.8794
0.7909	333.15	0.9130
0.8390	333.15	0.9341
0.8731	333.15	0.9484
0.9380	333.15	0.9752
1.0000	333.15	1.0000
0.0000	343.15	0.0000
0.0494	343.15	0.1589
0.1298	343.15	0.3420
0.1873	343.15	0.4414
0.2370	343.15	0.5121
0.2803	343.15	0.5623
0.3087	343.15	0.5902
0.3485	343.15	0.6268
0.4145	343.15	0.6864
0.5098	343.15	0.7546
0.6350	343.15	0.8281
0.6991	343.15	0.8600
0.7638	343.15	0.8920
0.8175	343.15	0.9178
0.8870	343.15	0.9503
0.9507	343.15	0.9785
1.0000	343.15	1.0000
0.0000	353.15	0.0000
0.0571	353.15	0.1867
0.1481	353.15	0.3820
0.1958	353.15	0.4571
0.2678	353.15	0.5483
0.3099	353.15	0.5903
0.3610	353.15	0.6372
0.3944	353.15	0.6612
0.5470	353.15	0.7661
0.6403	353.15	0.8192
0.7389	353.15	0.8705
0.8162	353.15	0.9083
0.8733	353.15	0.9358
0.9187	353.15	0.9578
0.9578	353.15	0.9779
1.0000	353.15	1.0000

Mole fraction of Isopropyl Alcohol (1) [ref]

Fixed		Measured
Mole fraction of Isopropyl Alcohol (1) - Liquid	Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Gas
0.0000	333.15	0.0000
0.0515	333.15	0.1695
0.1299	333.15	0.3521
0.1698	333.15	0.4235
0.2192	333.15	0.4992
0.2598	333.15	0.5499
0.3117	333.15	0.6073
0.3546	333.15	0.6470
0.3895	333.15	0.6773
0.4605	333.15	0.7319
0.5803	333.15	0.8061
0.7187	333.15	0.8794
0.7909	333.15	0.9130
0.8390	333.15	0.9341
0.8731	333.15	0.9484
0.9380	333.15	0.9752
1.0000	333.15	1.0000
0.0000	343.15	0.0000
0.0494	343.15	0.1589
0.1298	343.15	0.3420
0.1873	343.15	0.4414
0.2370	343.15	0.5121
0.2803	343.15	0.5623
0.3087	343.15	0.5902
0.3485	343.15	0.6268
0.4145	343.15	0.6864
0.5098	343.15	0.7546
0.6350	343.15	0.8281
0.6991	343.15	0.8600
0.7638	343.15	0.8920
0.8175	343.15	0.9178
0.8870	343.15	0.9503
0.9507	343.15	0.9785
1.0000	343.15	1.0000
0.0000	353.15	0.0000
0.0571	353.15	0.1867
0.1481	353.15	0.3820
0.1958	353.15	0.4571
0.2678	353.15	0.5483
0.3099	353.15	0.5903
0.3610	353.15	0.6372
0.3944	353.15	0.6612
0.5470	353.15	0.7661
0.6403	353.15	0.8192
0.7389	353.15	0.8705
0.8162	353.15	0.9083
0.8733	353.15	0.9358
0.9187	353.15	0.9578
0.9578	353.15	0.9779
1.0000	353.15	1.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.1495	0.0024
293.15	0.2001	0.0025
293.15	0.3000	0.0026
293.15	0.4249	0.0028
293.15	0.5189	0.0030
293.15	0.6202	0.0032
293.15	0.7166	0.0034
293.15	0.8005	0.0036
293.15	0.9001	0.0038
303.15	0.1495	0.0018
303.15	0.2001	0.0018
303.15	0.3000	0.0019
303.15	0.4249	0.0020
303.15	0.5189	0.0021
303.15	0.6202	0.0023
303.15	0.7166	0.0024
303.15	0.8005	0.0025
303.15	0.9001	0.0027
313.15	0.1495	0.0013
313.15	0.2001	0.0013
313.15	0.3000	0.0013
313.15	0.4249	0.0014
313.15	0.5189	0.0015
313.15	0.6202	0.0016
313.15	0.7166	0.0017
313.15	0.8005	0.0018
313.15	0.9001	0.0020
323.15	0.1495	0.0010
323.15	0.2001	0.0010
323.15	0.3000	0.0010
323.15	0.4249	0.0011
323.15	0.5189	0.0012
323.15	0.6202	0.0012
323.15	0.7166	0.0013
323.15	0.8005	0.0014
323.15	0.9001	0.0015
333.15	0.1495	0.0006
333.15	0.2001	0.0007
333.15	0.3000	0.0007
333.15	0.4249	0.0007
333.15	0.5189	0.0008
333.15	0.6202	0.0009
333.15	0.7166	0.0009
333.15	0.8005	0.0010
333.15	0.9001	0.0011

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.1495	0.0024
293.15	0.2001	0.0025
293.15	0.3000	0.0026
293.15	0.4249	0.0028
293.15	0.5189	0.0030
293.15	0.6202	0.0032
293.15	0.7166	0.0034
293.15	0.8005	0.0036
293.15	0.9001	0.0038
303.15	0.1495	0.0018
303.15	0.2001	0.0018
303.15	0.3000	0.0019
303.15	0.4249	0.0020
303.15	0.5189	0.0021
303.15	0.6202	0.0023
303.15	0.7166	0.0024
303.15	0.8005	0.0025
303.15	0.9001	0.0027
313.15	0.1495	0.0013
313.15	0.2001	0.0013
313.15	0.3000	0.0013
313.15	0.4249	0.0014
313.15	0.5189	0.0015
313.15	0.6202	0.0016
313.15	0.7166	0.0017
313.15	0.8005	0.0018
313.15	0.9001	0.0020
323.15	0.1495	0.0010
323.15	0.2001	0.0010
323.15	0.3000	0.0010
323.15	0.4249	0.0011
323.15	0.5189	0.0012
323.15	0.6202	0.0012
323.15	0.7166	0.0013
323.15	0.8005	0.0014
323.15	0.9001	0.0015
333.15	0.1495	0.0006
333.15	0.2001	0.0007
333.15	0.3000	0.0007
333.15	0.4249	0.0007
333.15	0.5189	0.0008
333.15	0.6202	0.0009
333.15	0.7166	0.0009
333.15	0.8005	0.0010
333.15	0.9001	0.0011

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Isopropyl Alcohol (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	333.15	12.30
0.0515	333.15	14.10
0.1299	333.15	16.60
0.1698	333.15	17.80
0.2192	333.15	19.30
0.2598	333.15	20.50
0.3117	333.15	21.90
0.3546	333.15	23.00
0.3895	333.15	23.90
0.4605	333.15	25.70
0.5803	333.15	28.50
0.7187	333.15	31.60
0.7909	333.15	33.50
0.8390	333.15	34.60
0.8731	333.15	35.50
0.9380	333.15	37.00
1.0000	333.15	38.50
0.0000	343.15	21.00
0.0494	343.15	23.70
0.1298	343.15	27.80
0.1873	343.15	30.60
0.2370	343.15	33.00
0.2803	343.15	34.80
0.3087	343.15	35.90
0.3485	343.15	37.30
0.4145	343.15	40.10
0.5098	343.15	43.40
0.6350	343.15	47.80
0.6991	343.15	50.00
0.7638	343.15	52.50
0.8175	343.15	54.50
0.8870	343.15	57.10
0.9507	343.15	59.40
1.0000	343.15	61.10
0.0000	353.15	32.70
0.0571	353.15	38.10
0.1481	353.15	45.40
0.1958	353.15	49.00
0.2678	353.15	53.70
0.3099	353.15	56.30
0.3610	353.15	59.50
0.3944	353.15	61.00
0.5470	353.15	68.50
0.6403	353.15	74.30
0.7389	353.15	79.90
0.8162	353.15	83.40
0.8733	353.15	86.40
0.9187	353.15	88.70
0.9578	353.15	90.50
1.0000	353.15	92.30

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Isopropyl Alcohol (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	333.15	12.30
0.0515	333.15	14.10
0.1299	333.15	16.60
0.1698	333.15	17.80
0.2192	333.15	19.30
0.2598	333.15	20.50
0.3117	333.15	21.90
0.3546	333.15	23.00
0.3895	333.15	23.90
0.4605	333.15	25.70
0.5803	333.15	28.50
0.7187	333.15	31.60
0.7909	333.15	33.50
0.8390	333.15	34.60
0.8731	333.15	35.50
0.9380	333.15	37.00
1.0000	333.15	38.50
0.0000	343.15	21.00
0.0494	343.15	23.70
0.1298	343.15	27.80
0.1873	343.15	30.60
0.2370	343.15	33.00
0.2803	343.15	34.80
0.3087	343.15	35.90
0.3485	343.15	37.30
0.4145	343.15	40.10
0.5098	343.15	43.40
0.6350	343.15	47.80
0.6991	343.15	50.00
0.7638	343.15	52.50
0.8175	343.15	54.50
0.8870	343.15	57.10
0.9507	343.15	59.40
1.0000	343.15	61.10
0.0000	353.15	32.70
0.0571	353.15	38.10
0.1481	353.15	45.40
0.1958	353.15	49.00
0.2678	353.15	53.70
0.3099	353.15	56.30
0.3610	353.15	59.50
0.3944	353.15	61.00
0.5470	353.15	68.50
0.6403	353.15	74.30
0.7389	353.15	79.90
0.8162	353.15	83.40
0.8733	353.15	86.40
0.9187	353.15	88.70
0.9578	353.15	90.50
1.0000	353.15	92.30

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Liquid	Mass density, kg/m3 - Liquid
333.15	0.0000	769.49
333.15	0.0420	768.8
333.15	0.1428	767.1
333.15	0.1913	766.26
333.15	0.2906	764.49
333.15	0.3911	762.62
333.15	0.4444	761.6
333.15	0.4993	760.52
333.15	0.5485	759.52
333.15	0.5940	758.58
333.15	0.6911	756.5
333.15	0.7445	755.31
333.15	0.8481	752.91
333.15	0.8925	751.85
333.15	0.9491	750.48
333.15	1.0000	749.23
343.15	0.0000	760.79
343.15	0.0420	760.07
343.15	0.1428	758.28
343.15	0.1913	757.39
343.15	0.2906	755.53
343.15	0.3911	753.57
343.15	0.4444	752.49
343.15	0.4993	751.36
343.15	0.5485	750.32
343.15	0.5940	749.33
343.15	0.6911	747.14
343.15	0.7445	745.88
343.15	0.8481	743.36
343.15	0.8925	742.24
343.15	0.9491	740.78
343.15	1.0000	739.46
353.15	0.0000	751.86
353.15	0.0420	751.1
353.15	0.1428	749.19
353.15	0.1913	748.25
353.15	0.2906	746.26
353.15	0.3911	744.18
353.15	0.4444	743.03
353.15	0.4993	741.83
353.15	0.5485	740.72
353.15	0.5940	739.66
353.15	0.6911	737.33
353.15	0.7445	735.99
353.15	0.8481	733.3
353.15	0.8925	732.1
353.15	0.9491	730.53
353.15	1.0000	729.1

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.1495	788.29
293.15	0.2001	789.25
293.15	0.3000	791.09
293.15	0.4249	793.26
293.15	0.5189	794.8
293.15	0.6202	796.38
293.15	0.7166	797.83
293.15	0.8005	799.06
293.15	0.9001	800.47
303.15	0.1495	779.93
303.15	0.2001	780.93
303.15	0.3000	782.85
303.15	0.4249	785.12
303.15	0.5189	786.73
303.15	0.6202	788.38
303.15	0.7166	789.9
303.15	0.8005	791.18
303.15	0.9001	792.65
313.15	0.1495	771.29
313.15	0.2001	772.34
313.15	0.3000	774.35
313.15	0.4249	776.74
313.15	0.5189	778.43
313.15	0.6202	780.17
313.15	0.7166	781.76
313.15	0.8005	783.1
313.15	0.9001	784.64
323.15	0.1495	762.29
323.15	0.2001	763.4
323.15	0.3000	765.53
323.15	0.4249	768.04
323.15	0.5189	769.83
323.15	0.6202	771.67
323.15	0.7166	773.35
323.15	0.8005	774.76
323.15	0.9001	776.38
333.15	0.1495	752.87
333.15	0.2001	754.05
333.15	0.3000	756.31
333.15	0.4249	758.97
333.15	0.5189	760.87
333.15	0.6202	762.82
333.15	0.7166	764.6
333.15	0.8005	766.09
333.15	0.9001	767.81

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Liquid	Mass density, kg/m3 - Liquid
333.15	0.0000	769.49
333.15	0.0420	768.8
333.15	0.1428	767.1
333.15	0.1913	766.26
333.15	0.2906	764.49
333.15	0.3911	762.62
333.15	0.4444	761.6
333.15	0.4993	760.52
333.15	0.5485	759.52
333.15	0.5940	758.58
333.15	0.6911	756.5
333.15	0.7445	755.31
333.15	0.8481	752.91
333.15	0.8925	751.85
333.15	0.9491	750.48
333.15	1.0000	749.23
343.15	0.0000	760.79
343.15	0.0420	760.07
343.15	0.1428	758.28
343.15	0.1913	757.39
343.15	0.2906	755.53
343.15	0.3911	753.57
343.15	0.4444	752.49
343.15	0.4993	751.36
343.15	0.5485	750.32
343.15	0.5940	749.33
343.15	0.6911	747.14
343.15	0.7445	745.88
343.15	0.8481	743.36
343.15	0.8925	742.24
343.15	0.9491	740.78
343.15	1.0000	739.46
353.15	0.0000	751.86
353.15	0.0420	751.1
353.15	0.1428	749.19
353.15	0.1913	748.25
353.15	0.2906	746.26
353.15	0.3911	744.18
353.15	0.4444	743.03
353.15	0.4993	741.83
353.15	0.5485	740.72
353.15	0.5940	739.66
353.15	0.6911	737.33
353.15	0.7445	735.99
353.15	0.8481	733.3
353.15	0.8925	732.1
353.15	0.9491	730.53
353.15	1.0000	729.1

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Propanol, 2-methyl- (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.1495	788.29
293.15	0.2001	789.25
293.15	0.3000	791.09
293.15	0.4249	793.26
293.15	0.5189	794.8
293.15	0.6202	796.38
293.15	0.7166	797.83
293.15	0.8005	799.06
293.15	0.9001	800.47
303.15	0.1495	779.93
303.15	0.2001	780.93
303.15	0.3000	782.85
303.15	0.4249	785.12
303.15	0.5189	786.73
303.15	0.6202	788.38
303.15	0.7166	789.9
303.15	0.8005	791.18
303.15	0.9001	792.65
313.15	0.1495	771.29
313.15	0.2001	772.34
313.15	0.3000	774.35
313.15	0.4249	776.74
313.15	0.5189	778.43
313.15	0.6202	780.17
313.15	0.7166	781.76
313.15	0.8005	783.1
313.15	0.9001	784.64
323.15	0.1495	762.29
323.15	0.2001	763.4
323.15	0.3000	765.53
323.15	0.4249	768.04
323.15	0.5189	769.83
323.15	0.6202	771.67
323.15	0.7166	773.35
323.15	0.8005	774.76
323.15	0.9001	776.38
333.15	0.1495	752.87
333.15	0.2001	754.05
333.15	0.3000	756.31
333.15	0.4249	758.97
333.15	0.5189	760.87
333.15	0.6202	762.82
333.15	0.7166	764.6
333.15	0.8005	766.09
333.15	0.9001	767.81

Sources

• Excess Properties and Phase Equilibria for the Potential Biofuel System of Propan-2-ol and 2-Methyl-propan-1-ol at 333.15, 343.15, and 353.15 K
• Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure