Mixture of 1-Butanol + 1,1'-Bicyclohexyl

Excel

1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3

1,1'-Bicyclohexyl

Name
1,1'-Bicyclohexyl
InChI
InChI=1S/C12H22/c1-3-7-11(8-4-1)12-9-5-2-6-10-12/h11-12H,1-10H2
InChI Key
WVIIMZNLDWSIRH-UHFFFAOYSA-N
Formula
C12H22
SMILES
C1CCC(C2CCCCC2)CC1
Mol. Weight (g/mol)
166.30
CAS
92-51-3
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Datasets

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

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,1'-Bicyclohexyl (2) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0029
293.15 0.1007 0.0029
293.15 0.2009 0.0029
293.15 0.3021 0.0029
293.15 0.4007 0.0030
293.15 0.5038 0.0030
293.15 0.5992 0.0031
293.15 0.7006 0.0032
293.15 0.7983 0.0034
293.15 0.8835 0.0036
293.15 1.0000 0.0040
298.15 0.0000 0.0026
298.15 0.1007 0.0025
298.15 0.2009 0.0025
298.15 0.3021 0.0025
298.15 0.4007 0.0026
298.15 0.5038 0.0026
298.15 0.5992 0.0027
298.15 0.7006 0.0029
298.15 0.7983 0.0030
298.15 0.8835 0.0032
298.15 1.0000 0.0035
303.15 0.0000 0.0023
303.15 0.1007 0.0022
303.15 0.2009 0.0022
303.15 0.3021 0.0023
303.15 0.4007 0.0023
303.15 0.5038 0.0024
303.15 0.5992 0.0024
303.15 0.7006 0.0025
303.15 0.7983 0.0027
303.15 0.8835 0.0028
303.15 1.0000 0.0031
308.15 0.0000 0.0020
308.15 0.1007 0.0020
308.15 0.2009 0.0020
308.15 0.3021 0.0020
308.15 0.4007 0.0021
308.15 0.5038 0.0021
308.15 0.5992 0.0022
308.15 0.7006 0.0023
308.15 0.7983 0.0024
308.15 0.8835 0.0025
308.15 1.0000 0.0028
313.15 0.0000 0.0018
313.15 0.1007 0.0017
313.15 0.2009 0.0018
313.15 0.3021 0.0018
313.15 0.4007 0.0018
313.15 0.5038 0.0019
313.15 0.5992 0.0020
313.15 0.7006 0.0020
313.15 0.7983 0.0022
313.15 0.8835 0.0023
313.15 1.0000 0.0025
318.15 0.0000 0.0016
318.15 0.1007 0.0016
318.15 0.2009 0.0016
318.15 0.3021 0.0016
318.15 0.4007 0.0017
318.15 0.5038 0.0017
318.15 0.5992 0.0018
318.15 0.7006 0.0019
318.15 0.7983 0.0020
318.15 0.8835 0.0020
318.15 1.0000 0.0023
323.15 0.0000 0.0014
323.15 0.1007 0.0014
323.15 0.2009 0.0014
323.15 0.3021 0.0015
323.15 0.4007 0.0015
323.15 0.5038 0.0015
323.15 0.5992 0.0016
323.15 0.7006 0.0017
323.15 0.7983 0.0018
323.15 0.8835 0.0019
323.15 1.0000 0.0021
328.15 0.0000 0.0013
328.15 0.1007 0.0013
328.15 0.2009 0.0013
328.15 0.3021 0.0013
328.15 0.4007 0.0014
328.15 0.5038 0.0014
328.15 0.5992 0.0015
328.15 0.7006 0.0015
328.15 0.7983 0.0016
328.15 0.8835 0.0017
328.15 1.0000 0.0019
333.15 0.0000 0.0012
333.15 0.1007 0.0011
333.15 0.2009 0.0012
333.15 0.3021 0.0012
333.15 0.4007 0.0012
333.15 0.5038 0.0013
333.15 0.5992 0.0013
333.15 0.7006 0.0014
333.15 0.7983 0.0015
333.15 0.8835 0.0016
333.15 1.0000 0.0018

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,1'-Bicyclohexyl (2) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0029
293.15 0.1007 0.0029
293.15 0.2009 0.0029
293.15 0.3021 0.0029
293.15 0.4007 0.0030
293.15 0.5038 0.0030
293.15 0.5992 0.0031
293.15 0.7006 0.0032
293.15 0.7983 0.0034
293.15 0.8835 0.0036
293.15 1.0000 0.0040
298.15 0.0000 0.0026
298.15 0.1007 0.0025
298.15 0.2009 0.0025
298.15 0.3021 0.0025
298.15 0.4007 0.0026
298.15 0.5038 0.0026
298.15 0.5992 0.0027
298.15 0.7006 0.0029
298.15 0.7983 0.0030
298.15 0.8835 0.0032
298.15 1.0000 0.0035
303.15 0.0000 0.0023
303.15 0.1007 0.0022
303.15 0.2009 0.0022
303.15 0.3021 0.0023
303.15 0.4007 0.0023
303.15 0.5038 0.0024
303.15 0.5992 0.0024
303.15 0.7006 0.0025
303.15 0.7983 0.0027
303.15 0.8835 0.0028
303.15 1.0000 0.0031
308.15 0.0000 0.0020
308.15 0.1007 0.0020
308.15 0.2009 0.0020
308.15 0.3021 0.0020
308.15 0.4007 0.0021
308.15 0.5038 0.0021
308.15 0.5992 0.0022
308.15 0.7006 0.0023
308.15 0.7983 0.0024
308.15 0.8835 0.0025
308.15 1.0000 0.0028
313.15 0.0000 0.0018
313.15 0.1007 0.0017
313.15 0.2009 0.0018
313.15 0.3021 0.0018
313.15 0.4007 0.0018
313.15 0.5038 0.0019
313.15 0.5992 0.0020
313.15 0.7006 0.0020
313.15 0.7983 0.0022
313.15 0.8835 0.0023
313.15 1.0000 0.0025
318.15 0.0000 0.0016
318.15 0.1007 0.0016
318.15 0.2009 0.0016
318.15 0.3021 0.0016
318.15 0.4007 0.0017
318.15 0.5038 0.0017
318.15 0.5992 0.0018
318.15 0.7006 0.0019
318.15 0.7983 0.0020
318.15 0.8835 0.0020
318.15 1.0000 0.0023
323.15 0.0000 0.0014
323.15 0.1007 0.0014
323.15 0.2009 0.0014
323.15 0.3021 0.0015
323.15 0.4007 0.0015
323.15 0.5038 0.0015
323.15 0.5992 0.0016
323.15 0.7006 0.0017
323.15 0.7983 0.0018
323.15 0.8835 0.0019
323.15 1.0000 0.0021
328.15 0.0000 0.0013
328.15 0.1007 0.0013
328.15 0.2009 0.0013
328.15 0.3021 0.0013
328.15 0.4007 0.0014
328.15 0.5038 0.0014
328.15 0.5992 0.0015
328.15 0.7006 0.0015
328.15 0.7983 0.0016
328.15 0.8835 0.0017
328.15 1.0000 0.0019
333.15 0.0000 0.0012
333.15 0.1007 0.0011
333.15 0.2009 0.0012
333.15 0.3021 0.0012
333.15 0.4007 0.0012
333.15 0.5038 0.0013
333.15 0.5992 0.0013
333.15 0.7006 0.0014
333.15 0.7983 0.0015
333.15 0.8835 0.0016
333.15 1.0000 0.0018

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,1'-Bicyclohexyl (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 809.5
293.15 0.1007 823.66
293.15 0.2009 835.23
293.15 0.3021 845.04
293.15 0.4007 853.19
293.15 0.5038 860.51
293.15 0.5992 866.48
293.15 0.7006 872.11
293.15 0.7983 877.03
293.15 0.8835 880.86
293.15 1.0000 886.05
298.15 0.0000 805.7
298.15 0.1007 819.86
298.15 0.2009 831.42
298.15 0.3021 841.24
298.15 0.4007 849.39
298.15 0.5038 856.73
298.15 0.5992 862.71
298.15 0.7006 868.37
298.15 0.7983 873.33
298.15 0.8835 877.19
298.15 1.0000 882.44
303.15 0.0000 801.87
303.15 0.1007 816.02
303.15 0.2009 827.58
303.15 0.3021 837.4
303.15 0.4007 845.56
303.15 0.5038 852.92
303.15 0.5992 858.93
303.15 0.7006 864.61
303.15 0.7983 869.6
303.15 0.8835 873.49
303.15 1.0000 878.84
308.15 0.0000 798.0
308.15 0.1007 812.14
308.15 0.2009 823.71
308.15 0.3021 833.53
308.15 0.4007 841.7
308.15 0.5038 849.08
308.15 0.5992 855.12
308.15 0.7006 860.84
308.15 0.7983 865.87
308.15 0.8835 869.8
308.15 1.0000 875.25
313.15 0.0000 794.1
313.15 0.1007 808.22
313.15 0.2009 819.81
313.15 0.3021 829.63
313.15 0.4007 837.81
313.15 0.5038 845.22
313.15 0.5992 851.3
313.15 0.7006 857.05
313.15 0.7983 862.13
313.15 0.8835 866.09
313.15 1.0000 871.66
318.15 0.0000 790.15
318.15 0.1007 804.27
318.15 0.2009 815.86
318.15 0.3021 825.69
318.15 0.4007 833.9
318.15 0.5038 841.34
318.15 0.5992 847.45
318.15 0.7006 853.25
318.15 0.7983 858.37
318.15 0.8835 862.38
318.15 1.0000 868.08
323.15 0.0000 786.16
323.15 0.1007 800.27
323.15 0.2009 811.87
323.15 0.3021 821.71
323.15 0.4007 829.95
323.15 0.5038 837.43
323.15 0.5992 843.58
323.15 0.7006 849.43
323.15 0.7983 854.6
323.15 0.8835 858.66
323.15 1.0000 864.5
328.15 0.0000 782.12
328.15 0.1007 796.21
328.15 0.2009 807.82
328.15 0.3021 817.69
328.15 0.4007 825.97
328.15 0.5038 833.49
328.15 0.5992 839.69
328.15 0.7006 845.59
328.15 0.7983 850.82
328.15 0.8835 854.93
328.15 1.0000 860.93
333.15 0.0000 778.01
333.15 0.1007 792.1
333.15 0.2009 803.73
333.15 0.3021 813.63
333.15 0.4007 821.94
333.15 0.5038 829.52
333.15 0.5992 835.77
333.15 0.7006 841.73
333.15 0.7983 847.02
333.15 0.8835 851.2
333.15 1.0000 857.35

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,1'-Bicyclohexyl (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 809.5
293.15 0.1007 823.66
293.15 0.2009 835.23
293.15 0.3021 845.04
293.15 0.4007 853.19
293.15 0.5038 860.51
293.15 0.5992 866.48
293.15 0.7006 872.11
293.15 0.7983 877.03
293.15 0.8835 880.86
293.15 1.0000 886.05
298.15 0.0000 805.7
298.15 0.1007 819.86
298.15 0.2009 831.42
298.15 0.3021 841.24
298.15 0.4007 849.39
298.15 0.5038 856.73
298.15 0.5992 862.71
298.15 0.7006 868.37
298.15 0.7983 873.33
298.15 0.8835 877.19
298.15 1.0000 882.44
303.15 0.0000 801.87
303.15 0.1007 816.02
303.15 0.2009 827.58
303.15 0.3021 837.4
303.15 0.4007 845.56
303.15 0.5038 852.92
303.15 0.5992 858.93
303.15 0.7006 864.61
303.15 0.7983 869.6
303.15 0.8835 873.49
303.15 1.0000 878.84
308.15 0.0000 798.0
308.15 0.1007 812.14
308.15 0.2009 823.71
308.15 0.3021 833.53
308.15 0.4007 841.7
308.15 0.5038 849.08
308.15 0.5992 855.12
308.15 0.7006 860.84
308.15 0.7983 865.87
308.15 0.8835 869.8
308.15 1.0000 875.25
313.15 0.0000 794.1
313.15 0.1007 808.22
313.15 0.2009 819.81
313.15 0.3021 829.63
313.15 0.4007 837.81
313.15 0.5038 845.22
313.15 0.5992 851.3
313.15 0.7006 857.05
313.15 0.7983 862.13
313.15 0.8835 866.09
313.15 1.0000 871.66
318.15 0.0000 790.15
318.15 0.1007 804.27
318.15 0.2009 815.86
318.15 0.3021 825.69
318.15 0.4007 833.9
318.15 0.5038 841.34
318.15 0.5992 847.45
318.15 0.7006 853.25
318.15 0.7983 858.37
318.15 0.8835 862.38
318.15 1.0000 868.08
323.15 0.0000 786.16
323.15 0.1007 800.27
323.15 0.2009 811.87
323.15 0.3021 821.71
323.15 0.4007 829.95
323.15 0.5038 837.43
323.15 0.5992 843.58
323.15 0.7006 849.43
323.15 0.7983 854.6
323.15 0.8835 858.66
323.15 1.0000 864.5
328.15 0.0000 782.12
328.15 0.1007 796.21
328.15 0.2009 807.82
328.15 0.3021 817.69
328.15 0.4007 825.97
328.15 0.5038 833.49
328.15 0.5992 839.69
328.15 0.7006 845.59
328.15 0.7983 850.82
328.15 0.8835 854.93
328.15 1.0000 860.93
333.15 0.0000 778.01
333.15 0.1007 792.1
333.15 0.2009 803.73
333.15 0.3021 813.63
333.15 0.4007 821.94
333.15 0.5038 829.52
333.15 0.5992 835.77
333.15 0.7006 841.73
333.15 0.7983 847.02
333.15 0.8835 851.2
333.15 1.0000 857.35

Sources