Mixture of Cyclohexane, butyl- + Cyclopropyl carbinol

Datasets

1. η - Viscosity, Pa*s (2)
2. ρ_l - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of Cyclopropyl carbinol (2) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.0000	293.15	0.0013
0.1039	293.15	0.0013
0.2031	293.15	0.0014
0.3022	293.15	0.0015
0.3997	293.15	0.0016
0.4993	293.15	0.0018
0.5994	293.15	0.0020
0.7000	293.15	0.0023
0.7970	293.15	0.0027
0.9004	293.15	0.0032
1.0000	293.15	0.0040
0.0000	298.15	0.0012
0.1039	298.15	0.0012
0.2031	298.15	0.0013
0.3022	298.15	0.0013
0.3997	298.15	0.0015
0.4993	298.15	0.0016
0.5994	298.15	0.0018
0.7000	298.15	0.0020
0.7970	298.15	0.0024
0.9004	298.15	0.0028
1.0000	298.15	0.0035
0.0000	303.15	0.0011
0.1039	303.15	0.0011
0.2031	303.15	0.0012
0.3022	303.15	0.0012
0.3997	303.15	0.0013
0.4993	303.15	0.0014
0.5994	303.15	0.0016
0.7000	303.15	0.0018
0.7970	303.15	0.0021
0.9004	303.15	0.0025
1.0000	303.15	0.0030
0.0000	308.15	0.0010
0.1039	308.15	0.0010
0.2031	308.15	0.0011
0.3022	308.15	0.0011
0.3997	308.15	0.0012
0.4993	308.15	0.0013
0.5994	308.15	0.0014
0.7000	308.15	0.0016
0.7970	308.15	0.0019
0.9004	308.15	0.0022
1.0000	308.15	0.0027
0.0000	313.15	0.0010
0.1039	313.15	0.0010
0.2031	313.15	0.0010
0.3022	313.15	0.0010
0.3997	313.15	0.0011
0.4993	313.15	0.0012
0.5994	313.15	0.0013
0.7000	313.15	0.0015
0.7970	313.15	0.0017
0.9004	313.15	0.0019
1.0000	313.15	0.0023
0.0000	318.15	0.0009
0.1039	318.15	0.0009
0.2031	318.15	0.0009
0.3022	318.15	0.0010
0.3997	318.15	0.0010
0.4993	318.15	0.0011
0.5994	318.15	0.0012
0.7000	318.15	0.0013
0.7970	318.15	0.0015
0.9004	318.15	0.0017
1.0000	318.15	0.0021
0.0000	323.15	0.0008
0.1039	323.15	0.0008
0.2031	323.15	0.0009
0.3022	323.15	0.0009
0.3997	323.15	0.0009
0.4993	323.15	0.0010
0.5994	323.15	0.0011
0.7000	323.15	0.0012
0.7970	323.15	0.0013
0.9004	323.15	0.0016
1.0000	323.15	0.0018
0.0000	328.15	0.0008
0.1039	328.15	0.0008
0.2031	328.15	0.0008
0.3022	328.15	0.0008
0.3997	328.15	0.0009
0.4993	328.15	0.0009
0.5994	328.15	0.0010
0.7000	328.15	0.0011
0.7970	328.15	0.0012
0.9004	328.15	0.0014
1.0000	328.15	0.0016
0.0000	333.15	0.0007
0.1039	333.15	0.0007
0.2031	333.15	0.0008
0.3022	333.15	0.0008
0.3997	333.15	0.0008
0.4993	333.15	0.0009
0.5994	333.15	0.0009
0.7000	333.15	0.0010
0.7970	333.15	0.0011
0.9004	333.15	0.0013
1.0000	333.15	0.0015
0.0000	338.15	0.0007
0.1039	338.15	0.0007
0.2031	338.15	0.0007
0.3022	338.15	0.0007
0.3997	338.15	0.0008
0.4993	338.15	0.0008
0.5994	338.15	0.0009
0.7000	338.15	0.0009
0.7970	338.15	0.0010
0.9004	338.15	0.0011
1.0000	338.15	0.0013
0.0000	343.15	0.0007
0.1039	343.15	0.0007
0.2031	343.15	0.0007
0.3022	343.15	0.0007
0.3997	343.15	0.0007
0.4993	343.15	0.0007
0.5994	343.15	0.0008
0.7000	343.15	0.0008
0.7970	343.15	0.0009
0.9004	343.15	0.0010
1.0000	343.15	0.0012

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of Cyclopropyl carbinol (2) - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
0.0000	293.15	0.0013
0.1039	293.15	0.0013
0.2031	293.15	0.0014
0.3022	293.15	0.0015
0.3997	293.15	0.0016
0.4993	293.15	0.0018
0.5994	293.15	0.0020
0.7000	293.15	0.0023
0.7970	293.15	0.0027
0.9004	293.15	0.0032
1.0000	293.15	0.0040
0.0000	298.15	0.0012
0.1039	298.15	0.0012
0.2031	298.15	0.0013
0.3022	298.15	0.0013
0.3997	298.15	0.0015
0.4993	298.15	0.0016
0.5994	298.15	0.0018
0.7000	298.15	0.0020
0.7970	298.15	0.0024
0.9004	298.15	0.0028
1.0000	298.15	0.0035
0.0000	303.15	0.0011
0.1039	303.15	0.0011
0.2031	303.15	0.0012
0.3022	303.15	0.0012
0.3997	303.15	0.0013
0.4993	303.15	0.0014
0.5994	303.15	0.0016
0.7000	303.15	0.0018
0.7970	303.15	0.0021
0.9004	303.15	0.0025
1.0000	303.15	0.0030
0.0000	308.15	0.0010
0.1039	308.15	0.0010
0.2031	308.15	0.0011
0.3022	308.15	0.0011
0.3997	308.15	0.0012
0.4993	308.15	0.0013
0.5994	308.15	0.0014
0.7000	308.15	0.0016
0.7970	308.15	0.0019
0.9004	308.15	0.0022
1.0000	308.15	0.0027
0.0000	313.15	0.0010
0.1039	313.15	0.0010
0.2031	313.15	0.0010
0.3022	313.15	0.0010
0.3997	313.15	0.0011
0.4993	313.15	0.0012
0.5994	313.15	0.0013
0.7000	313.15	0.0015
0.7970	313.15	0.0017
0.9004	313.15	0.0019
1.0000	313.15	0.0023
0.0000	318.15	0.0009
0.1039	318.15	0.0009
0.2031	318.15	0.0009
0.3022	318.15	0.0010
0.3997	318.15	0.0010
0.4993	318.15	0.0011
0.5994	318.15	0.0012
0.7000	318.15	0.0013
0.7970	318.15	0.0015
0.9004	318.15	0.0017
1.0000	318.15	0.0021
0.0000	323.15	0.0008
0.1039	323.15	0.0008
0.2031	323.15	0.0009
0.3022	323.15	0.0009
0.3997	323.15	0.0009
0.4993	323.15	0.0010
0.5994	323.15	0.0011
0.7000	323.15	0.0012
0.7970	323.15	0.0013
0.9004	323.15	0.0016
1.0000	323.15	0.0018
0.0000	328.15	0.0008
0.1039	328.15	0.0008
0.2031	328.15	0.0008
0.3022	328.15	0.0008
0.3997	328.15	0.0009
0.4993	328.15	0.0009
0.5994	328.15	0.0010
0.7000	328.15	0.0011
0.7970	328.15	0.0012
0.9004	328.15	0.0014
1.0000	328.15	0.0016
0.0000	333.15	0.0007
0.1039	333.15	0.0007
0.2031	333.15	0.0008
0.3022	333.15	0.0008
0.3997	333.15	0.0008
0.4993	333.15	0.0009
0.5994	333.15	0.0009
0.7000	333.15	0.0010
0.7970	333.15	0.0011
0.9004	333.15	0.0013
1.0000	333.15	0.0015
0.0000	338.15	0.0007
0.1039	338.15	0.0007
0.2031	338.15	0.0007
0.3022	338.15	0.0007
0.3997	338.15	0.0008
0.4993	338.15	0.0008
0.5994	338.15	0.0009
0.7000	338.15	0.0009
0.7970	338.15	0.0010
0.9004	338.15	0.0011
1.0000	338.15	0.0013
0.0000	343.15	0.0007
0.1039	343.15	0.0007
0.2031	343.15	0.0007
0.3022	343.15	0.0007
0.3997	343.15	0.0007
0.4993	343.15	0.0007
0.5994	343.15	0.0008
0.7000	343.15	0.0008
0.7970	343.15	0.0009
0.9004	343.15	0.0010
1.0000	343.15	0.0012

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of Cyclopropyl carbinol (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	293.15	799.34
0.1039	293.15	803.82
0.2031	293.15	809.39
0.3022	293.15	815.9
0.3997	293.15	823.34
0.4993	293.15	832.12
0.5994	293.15	842.55
0.7000	293.15	855.1
0.7970	293.15	869.68
0.9004	293.15	889.05
1.0000	293.15	912.99
0.0000	298.15	795.59
0.1039	298.15	800.02
0.2031	298.15	805.52
0.3022	298.15	812.0
0.3997	298.15	819.39
0.4993	298.15	828.15
0.5994	298.15	838.56
0.7000	298.15	851.09
0.7970	298.15	865.66
0.9004	298.15	885.02
1.0000	298.15	908.94
0.0000	303.15	791.84
0.1039	303.15	796.16
0.2031	303.15	801.61
0.3022	303.15	808.04
0.3997	303.15	815.4
0.4993	303.15	824.14
0.5994	303.15	834.52
0.7000	303.15	847.04
0.7970	303.15	861.6
0.9004	303.15	880.95
1.0000	303.15	904.85
0.0000	308.15	788.07
0.1039	308.15	792.28
0.2031	308.15	797.68
0.3022	308.15	804.06
0.3997	308.15	811.39
0.4993	308.15	820.09
0.5994	308.15	830.45
0.7000	308.15	842.95
0.7970	308.15	857.5
0.9004	308.15	876.84
1.0000	308.15	900.74
0.0000	313.15	784.3
0.1039	313.15	788.38
0.2031	313.15	793.72
0.3022	313.15	800.06
0.3997	313.15	807.34
0.4993	313.15	816.02
0.5994	313.15	826.34
0.7000	313.15	838.82
0.7970	313.15	853.35
0.9004	313.15	872.69
1.0000	313.15	896.58
0.0000	318.15	780.52
0.1039	318.15	784.47
0.2031	318.15	789.74
0.3022	318.15	796.03
0.3997	318.15	803.27
0.4993	318.15	811.9
0.5994	318.15	822.19
0.7000	318.15	834.65
0.7970	318.15	849.17
0.9004	318.15	868.5
1.0000	318.15	892.38
0.0000	323.15	776.74
0.1039	323.15	780.53
0.2031	323.15	785.74
0.3022	323.15	791.97
0.3997	323.15	799.16
0.4993	323.15	807.75
0.5994	323.15	818.01
0.7000	323.15	830.44
0.7970	323.15	844.94
0.9004	323.15	864.26
1.0000	323.15	888.13
0.0000	328.15	772.93
0.1039	328.15	776.57
0.2031	328.15	781.71
0.3022	328.15	787.87
0.3997	328.15	795.01
0.4993	328.15	803.56
0.5994	328.15	813.78
0.7000	328.15	826.18
0.7970	328.15	840.66
0.9004	328.15	859.97
1.0000	328.15	883.84
0.0000	333.15	769.13
0.1039	333.15	772.6
0.2031	333.15	777.65
0.3022	333.15	783.75
0.3997	333.15	790.83
0.4993	333.15	799.33
0.5994	333.15	809.5
0.7000	333.15	821.87
0.7970	333.15	836.33
0.9004	333.15	855.62
1.0000	333.15	879.49
0.0000	338.15	765.3
0.1039	338.15	768.6
0.2031	338.15	773.56
0.3022	338.15	779.59
0.3997	338.15	786.61
0.4993	338.15	795.05
0.5994	338.15	805.18
0.7000	338.15	817.51
0.7970	338.15	831.94
0.9004	338.15	851.21
1.0000	338.15	875.07
0.0000	343.15	761.47
0.1039	343.15	764.58
0.2031	343.15	769.4
0.3022	343.15	775.39
0.3997	343.15	782.35
0.4993	343.15	790.73
0.5994	343.15	800.8
0.7000	343.15	813.09
0.7970	343.15	827.49
0.9004	343.15	846.74
1.0000	343.15	870.62

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Mole fraction of Cyclopropyl carbinol (2) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	293.15	799.34
0.1039	293.15	803.82
0.2031	293.15	809.39
0.3022	293.15	815.9
0.3997	293.15	823.34
0.4993	293.15	832.12
0.5994	293.15	842.55
0.7000	293.15	855.1
0.7970	293.15	869.68
0.9004	293.15	889.05
1.0000	293.15	912.99
0.0000	298.15	795.59
0.1039	298.15	800.02
0.2031	298.15	805.52
0.3022	298.15	812.0
0.3997	298.15	819.39
0.4993	298.15	828.15
0.5994	298.15	838.56
0.7000	298.15	851.09
0.7970	298.15	865.66
0.9004	298.15	885.02
1.0000	298.15	908.94
0.0000	303.15	791.84
0.1039	303.15	796.16
0.2031	303.15	801.61
0.3022	303.15	808.04
0.3997	303.15	815.4
0.4993	303.15	824.14
0.5994	303.15	834.52
0.7000	303.15	847.04
0.7970	303.15	861.6
0.9004	303.15	880.95
1.0000	303.15	904.85
0.0000	308.15	788.07
0.1039	308.15	792.28
0.2031	308.15	797.68
0.3022	308.15	804.06
0.3997	308.15	811.39
0.4993	308.15	820.09
0.5994	308.15	830.45
0.7000	308.15	842.95
0.7970	308.15	857.5
0.9004	308.15	876.84
1.0000	308.15	900.74
0.0000	313.15	784.3
0.1039	313.15	788.38
0.2031	313.15	793.72
0.3022	313.15	800.06
0.3997	313.15	807.34
0.4993	313.15	816.02
0.5994	313.15	826.34
0.7000	313.15	838.82
0.7970	313.15	853.35
0.9004	313.15	872.69
1.0000	313.15	896.58
0.0000	318.15	780.52
0.1039	318.15	784.47
0.2031	318.15	789.74
0.3022	318.15	796.03
0.3997	318.15	803.27
0.4993	318.15	811.9
0.5994	318.15	822.19
0.7000	318.15	834.65
0.7970	318.15	849.17
0.9004	318.15	868.5
1.0000	318.15	892.38
0.0000	323.15	776.74
0.1039	323.15	780.53
0.2031	323.15	785.74
0.3022	323.15	791.97
0.3997	323.15	799.16
0.4993	323.15	807.75
0.5994	323.15	818.01
0.7000	323.15	830.44
0.7970	323.15	844.94
0.9004	323.15	864.26
1.0000	323.15	888.13
0.0000	328.15	772.93
0.1039	328.15	776.57
0.2031	328.15	781.71
0.3022	328.15	787.87
0.3997	328.15	795.01
0.4993	328.15	803.56
0.5994	328.15	813.78
0.7000	328.15	826.18
0.7970	328.15	840.66
0.9004	328.15	859.97
1.0000	328.15	883.84
0.0000	333.15	769.13
0.1039	333.15	772.6
0.2031	333.15	777.65
0.3022	333.15	783.75
0.3997	333.15	790.83
0.4993	333.15	799.33
0.5994	333.15	809.5
0.7000	333.15	821.87
0.7970	333.15	836.33
0.9004	333.15	855.62
1.0000	333.15	879.49
0.0000	338.15	765.3
0.1039	338.15	768.6
0.2031	338.15	773.56
0.3022	338.15	779.59
0.3997	338.15	786.61
0.4993	338.15	795.05
0.5994	338.15	805.18
0.7000	338.15	817.51
0.7970	338.15	831.94
0.9004	338.15	851.21
1.0000	338.15	875.07
0.0000	343.15	761.47
0.1039	343.15	764.58
0.2031	343.15	769.4
0.3022	343.15	775.39
0.3997	343.15	782.35
0.4993	343.15	790.73
0.5994	343.15	800.8
0.7000	343.15	813.09
0.7970	343.15	827.49
0.9004	343.15	846.74
1.0000	343.15	870.62

Sources

• Densities and Viscosities for the Ternary System of Cyclopropanemethanol (1) + n-Dodecane (2) + Butylcyclohexane (3) and Corresponding Binaries at T = 293.15 343.15 K