Mixture of Styrene + Octane

Excel

Styrene

Name
Styrene
InChI
InChI=1S/C8H8/c1-2-8-6-4-3-5-7-8/h2-7H,1H2
InChI Key
PPBRXRYQALVLMV-UHFFFAOYSA-N
Formula
C8H8
SMILES
C=Cc1ccccc1
Mol. Weight (g/mol)
104.15
CAS
100-42-5

Octane

Name
Octane
InChI
InChI=1S/C8H18/c1-3-5-7-8-6-4-2/h3-8H2,1-2H3
InChI Key
TVMXDCGIABBOFY-UHFFFAOYSA-N
Formula
C8H18
SMILES
CCCCCCCC
Mol. Weight (g/mol)
114.23
CAS
111-65-9
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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 = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Styrene (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0005
293.15 0.1085 0.0005
293.15 0.2151 0.0005
293.15 0.3202 0.0005
293.15 0.4223 0.0006
293.15 0.5230 0.0006
293.15 0.6220 0.0006
293.15 0.7189 0.0006
293.15 0.8145 0.0006
293.15 0.9081 0.0007
293.15 1.0000 0.0007
298.15 0.0000 0.0005
298.15 0.1085 0.0005
298.15 0.2151 0.0005
298.15 0.3202 0.0005
298.15 0.4223 0.0005
298.15 0.5230 0.0005
298.15 0.6220 0.0006
298.15 0.7189 0.0006
298.15 0.8145 0.0006
298.15 0.9081 0.0006
298.15 1.0000 0.0007
303.15 0.0000 0.0005
303.15 0.1085 0.0005
303.15 0.2151 0.0005
303.15 0.3202 0.0005
303.15 0.4223 0.0005
303.15 0.5230 0.0005
303.15 0.6220 0.0005
303.15 0.7189 0.0005
303.15 0.8145 0.0006
303.15 0.9081 0.0006
303.15 1.0000 0.0007
313.15 0.0000 0.0004
313.15 0.1085 0.0004
313.15 0.2151 0.0004
313.15 0.3202 0.0004
313.15 0.4223 0.0004
313.15 0.5230 0.0005
313.15 0.6220 0.0005
313.15 0.7189 0.0005
313.15 0.8145 0.0005
313.15 0.9081 0.0005
313.15 1.0000 0.0006
323.15 0.0000 0.0004
323.15 0.1085 0.0004
323.15 0.2151 0.0004
323.15 0.3202 0.0004
323.15 0.4223 0.0004
323.15 0.5230 0.0004
323.15 0.6220 0.0004
323.15 0.7189 0.0004
323.15 0.8145 0.0005
323.15 0.9081 0.0005
323.15 1.0000 0.0005
333.15 0.0000 0.0003
333.15 0.1085 0.0004
333.15 0.2151 0.0004
333.15 0.3202 0.0004
333.15 0.4223 0.0004
333.15 0.5230 0.0004
333.15 0.6220 0.0004
333.15 0.7189 0.0004
333.15 0.8145 0.0004
333.15 0.9081 0.0004
333.15 1.0000 0.0005
343.15 0.0000 0.0003
343.15 0.1085 0.0003
343.15 0.2151 0.0003
343.15 0.3202 0.0003
343.15 0.4223 0.0003
343.15 0.5230 0.0003
343.15 0.6220 0.0004
343.15 0.7189 0.0004
343.15 0.8145 0.0004
343.15 0.9081 0.0004
343.15 1.0000 0.0004
353.15 0.0000 0.0003
353.15 0.1085 0.0003
353.15 0.2151 0.0003
353.15 0.3202 0.0003
353.15 0.4223 0.0003
353.15 0.5230 0.0003
353.15 0.6220 0.0003
353.15 0.7189 0.0003
353.15 0.8145 0.0003
353.15 0.9081 0.0004
353.15 1.0000 0.0004
363.15 0.0000 0.0003
363.15 0.1085 0.0003
363.15 0.2151 0.0003
363.15 0.3202 0.0003
363.15 0.4223 0.0003
363.15 0.5230 0.0003
363.15 0.6220 0.0003
363.15 0.7189 0.0003
363.15 0.8145 0.0003
363.15 0.9081 0.0003
363.15 1.0000 0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Styrene (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0005
293.15 0.1085 0.0005
293.15 0.2151 0.0005
293.15 0.3202 0.0005
293.15 0.4223 0.0006
293.15 0.5230 0.0006
293.15 0.6220 0.0006
293.15 0.7189 0.0006
293.15 0.8145 0.0006
293.15 0.9081 0.0007
293.15 1.0000 0.0007
298.15 0.0000 0.0005
298.15 0.1085 0.0005
298.15 0.2151 0.0005
298.15 0.3202 0.0005
298.15 0.4223 0.0005
298.15 0.5230 0.0005
298.15 0.6220 0.0006
298.15 0.7189 0.0006
298.15 0.8145 0.0006
298.15 0.9081 0.0006
298.15 1.0000 0.0007
303.15 0.0000 0.0005
303.15 0.1085 0.0005
303.15 0.2151 0.0005
303.15 0.3202 0.0005
303.15 0.4223 0.0005
303.15 0.5230 0.0005
303.15 0.6220 0.0005
303.15 0.7189 0.0005
303.15 0.8145 0.0006
303.15 0.9081 0.0006
303.15 1.0000 0.0007
313.15 0.0000 0.0004
313.15 0.1085 0.0004
313.15 0.2151 0.0004
313.15 0.3202 0.0004
313.15 0.4223 0.0004
313.15 0.5230 0.0005
313.15 0.6220 0.0005
313.15 0.7189 0.0005
313.15 0.8145 0.0005
313.15 0.9081 0.0005
313.15 1.0000 0.0006
323.15 0.0000 0.0004
323.15 0.1085 0.0004
323.15 0.2151 0.0004
323.15 0.3202 0.0004
323.15 0.4223 0.0004
323.15 0.5230 0.0004
323.15 0.6220 0.0004
323.15 0.7189 0.0004
323.15 0.8145 0.0005
323.15 0.9081 0.0005
323.15 1.0000 0.0005
333.15 0.0000 0.0003
333.15 0.1085 0.0004
333.15 0.2151 0.0004
333.15 0.3202 0.0004
333.15 0.4223 0.0004
333.15 0.5230 0.0004
333.15 0.6220 0.0004
333.15 0.7189 0.0004
333.15 0.8145 0.0004
333.15 0.9081 0.0004
333.15 1.0000 0.0005
343.15 0.0000 0.0003
343.15 0.1085 0.0003
343.15 0.2151 0.0003
343.15 0.3202 0.0003
343.15 0.4223 0.0003
343.15 0.5230 0.0003
343.15 0.6220 0.0004
343.15 0.7189 0.0004
343.15 0.8145 0.0004
343.15 0.9081 0.0004
343.15 1.0000 0.0004
353.15 0.0000 0.0003
353.15 0.1085 0.0003
353.15 0.2151 0.0003
353.15 0.3202 0.0003
353.15 0.4223 0.0003
353.15 0.5230 0.0003
353.15 0.6220 0.0003
353.15 0.7189 0.0003
353.15 0.8145 0.0003
353.15 0.9081 0.0004
353.15 1.0000 0.0004
363.15 0.0000 0.0003
363.15 0.1085 0.0003
363.15 0.2151 0.0003
363.15 0.3202 0.0003
363.15 0.4223 0.0003
363.15 0.5230 0.0003
363.15 0.6220 0.0003
363.15 0.7189 0.0003
363.15 0.8145 0.0003
363.15 0.9081 0.0003
363.15 1.0000 0.0003

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Styrene (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 703.88
293.15 0.1085 719.52
293.15 0.2151 736.18
293.15 0.3202 753.7
293.15 0.4223 772.01
293.15 0.5230 791.51
293.15 0.6220 812.07
293.15 0.7189 833.64
293.15 0.8145 856.59
293.15 0.9081 880.84
293.15 1.0000 906.29
298.15 0.0000 699.83
298.15 0.1085 715.45
298.15 0.2151 732.06
298.15 0.3202 749.53
298.15 0.4223 767.81
298.15 0.5230 787.27
298.15 0.6220 807.78
298.15 0.7189 829.3
298.15 0.8145 852.22
298.15 0.9081 876.43
298.15 1.0000 901.86
303.15 0.0000 695.79
303.15 0.1085 711.38
303.15 0.2151 727.94
303.15 0.3202 745.38
303.15 0.4223 763.63
303.15 0.5230 783.03
303.15 0.6220 803.5
303.15 0.7189 824.98
303.15 0.8145 847.87
303.15 0.9081 872.03
303.15 1.0000 897.45
313.15 0.0000 687.59
313.15 0.1085 703.13
313.15 0.2151 719.6
313.15 0.3202 737.0
313.15 0.4223 755.16
313.15 0.5230 774.46
313.15 0.6220 794.86
313.15 0.7189 816.28
313.15 0.8145 839.09
313.15 0.9081 863.15
313.15 1.0000 888.53
323.15 0.0000 679.34
323.15 0.1085 694.84
323.15 0.2151 711.23
323.15 0.3202 728.58
323.15 0.4223 746.66
323.15 0.5230 765.88
323.15 0.6220 786.22
323.15 0.7189 807.56
323.15 0.8145 830.31
323.15 0.9081 854.31
323.15 1.0000 879.62
333.15 0.0000 670.98
333.15 0.1085 686.43
333.15 0.2151 702.74
333.15 0.3202 720.06
333.15 0.4223 738.07
333.15 0.5230 757.21
333.15 0.6220 777.49
333.15 0.7189 798.77
333.15 0.8145 821.46
333.15 0.9081 845.37
333.15 1.0000 870.64
343.15 0.0000 662.59
343.15 0.1085 677.99
343.15 0.2151 694.24
343.15 0.3202 711.51
343.15 0.4223 729.46
343.15 0.5230 748.55
343.15 0.6220 768.75
343.15 0.7189 789.97
343.15 0.8145 812.63
343.15 0.9081 836.5
343.15 1.0000 861.72
353.15 0.0000 654.05
353.15 0.1085 669.39
353.15 0.2151 685.6
353.15 0.3202 702.81
353.15 0.4223 720.71
353.15 0.5230 739.76
353.15 0.6220 759.93
353.15 0.7189 781.11
353.15 0.8145 803.68
353.15 0.9081 827.51
353.15 1.0000 852.68
363.15 0.0000 645.68
363.15 0.1085 660.98
363.15 0.2151 677.15
363.15 0.3202 694.32
363.15 0.4223 712.19
363.15 0.5230 731.2
363.15 0.6220 751.34
363.15 0.7189 772.48
363.15 0.8145 795.04
363.15 0.9081 818.82
363.15 1.0000 843.99

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Styrene (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 703.88
293.15 0.1085 719.52
293.15 0.2151 736.18
293.15 0.3202 753.7
293.15 0.4223 772.01
293.15 0.5230 791.51
293.15 0.6220 812.07
293.15 0.7189 833.64
293.15 0.8145 856.59
293.15 0.9081 880.84
293.15 1.0000 906.29
298.15 0.0000 699.83
298.15 0.1085 715.45
298.15 0.2151 732.06
298.15 0.3202 749.53
298.15 0.4223 767.81
298.15 0.5230 787.27
298.15 0.6220 807.78
298.15 0.7189 829.3
298.15 0.8145 852.22
298.15 0.9081 876.43
298.15 1.0000 901.86
303.15 0.0000 695.79
303.15 0.1085 711.38
303.15 0.2151 727.94
303.15 0.3202 745.38
303.15 0.4223 763.63
303.15 0.5230 783.03
303.15 0.6220 803.5
303.15 0.7189 824.98
303.15 0.8145 847.87
303.15 0.9081 872.03
303.15 1.0000 897.45
313.15 0.0000 687.59
313.15 0.1085 703.13
313.15 0.2151 719.6
313.15 0.3202 737.0
313.15 0.4223 755.16
313.15 0.5230 774.46
313.15 0.6220 794.86
313.15 0.7189 816.28
313.15 0.8145 839.09
313.15 0.9081 863.15
313.15 1.0000 888.53
323.15 0.0000 679.34
323.15 0.1085 694.84
323.15 0.2151 711.23
323.15 0.3202 728.58
323.15 0.4223 746.66
323.15 0.5230 765.88
323.15 0.6220 786.22
323.15 0.7189 807.56
323.15 0.8145 830.31
323.15 0.9081 854.31
323.15 1.0000 879.62
333.15 0.0000 670.98
333.15 0.1085 686.43
333.15 0.2151 702.74
333.15 0.3202 720.06
333.15 0.4223 738.07
333.15 0.5230 757.21
333.15 0.6220 777.49
333.15 0.7189 798.77
333.15 0.8145 821.46
333.15 0.9081 845.37
333.15 1.0000 870.64
343.15 0.0000 662.59
343.15 0.1085 677.99
343.15 0.2151 694.24
343.15 0.3202 711.51
343.15 0.4223 729.46
343.15 0.5230 748.55
343.15 0.6220 768.75
343.15 0.7189 789.97
343.15 0.8145 812.63
343.15 0.9081 836.5
343.15 1.0000 861.72
353.15 0.0000 654.05
353.15 0.1085 669.39
353.15 0.2151 685.6
353.15 0.3202 702.81
353.15 0.4223 720.71
353.15 0.5230 739.76
353.15 0.6220 759.93
353.15 0.7189 781.11
353.15 0.8145 803.68
353.15 0.9081 827.51
353.15 1.0000 852.68
363.15 0.0000 645.68
363.15 0.1085 660.98
363.15 0.2151 677.15
363.15 0.3202 694.32
363.15 0.4223 712.19
363.15 0.5230 731.2
363.15 0.6220 751.34
363.15 0.7189 772.48
363.15 0.8145 795.04
363.15 0.9081 818.82
363.15 1.0000 843.99

Sources