Mixture of p-Xylene + Heptane

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p-Xylene

Name
p-Xylene
InChI
InChI=1S/C8H10/c1-7-3-5-8(2)6-4-7/h3-6H,1-2H3
InChI Key
URLKBWYHVLBVBO-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1ccc(C)cc1
Mol. Weight (g/mol)
106.17
CAS
106-42-3

Heptane

Name
Heptane
InChI
InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3
InChI Key
IMNFDUFMRHMDMM-UHFFFAOYSA-N
Formula
C7H16
SMILES
CCCCCCC
Mol. Weight (g/mol)
100.20
CAS
142-82-5
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Datasets

  1. Mole fraction (2)
  2. η - Viscosity, Pa*s (2)
  3. Pvap - Vapor or sublimation pressure, kPa (2)
  4. ρl - Mass density, kg/m3 (2)

Mole fraction of Heptane (2) [ref]

Fixed Measured
Mole fraction of Heptane (2) - Liquid Temperature, K - Liquid Mole fraction of Heptane (2) - Gas
0.1795 323.20 0.5688
0.3708 323.20 0.7251
0.5793 323.20 0.8558
0.7845 323.20 0.9299
0.1891 343.20 0.5571
0.3689 343.20 0.7154
0.5757 343.20 0.8449
0.7734 343.20 0.9111
0.1856 363.20 0.5211
0.3568 363.20 0.6922
0.5749 363.20 0.8395
0.7694 363.20 0.9005

Mole fraction of Heptane (2) [ref]

Fixed Measured
Mole fraction of Heptane (2) - Liquid Temperature, K - Liquid Mole fraction of Heptane (2) - Gas
0.1795 323.20 0.5688
0.3708 323.20 0.7251
0.5793 323.20 0.8558
0.7845 323.20 0.9299
0.1891 343.20 0.5571
0.3689 343.20 0.7154
0.5757 343.20 0.8449
0.7734 343.20 0.9111
0.1856 363.20 0.5211
0.3568 363.20 0.6922
0.5749 363.20 0.8395
0.7694 363.20 0.9005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of p-Xylene (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0000 0.0004
298.15 0.0948 0.0004
298.15 0.1911 0.0004
298.15 0.2880 0.0004
298.15 0.3865 0.0004
298.15 0.4856 0.0005
298.15 0.5861 0.0005
298.15 0.6877 0.0005
298.15 0.7906 0.0005
298.15 0.8949 0.0006
298.15 1.0000 0.0006
303.15 0.0000 0.0004
303.15 0.0948 0.0004
303.15 0.1911 0.0004
303.15 0.2880 0.0004
303.15 0.3865 0.0004
303.15 0.4856 0.0004
303.15 0.5861 0.0004
303.15 0.6877 0.0005
303.15 0.7906 0.0005
303.15 0.8949 0.0005
303.15 1.0000 0.0006
313.15 0.0000 0.0003
313.15 0.0948 0.0003
313.15 0.1911 0.0004
313.15 0.2880 0.0004
313.15 0.3865 0.0004
313.15 0.4856 0.0004
313.15 0.5861 0.0004
313.15 0.6877 0.0004
313.15 0.7906 0.0004
313.15 0.8949 0.0005
313.15 1.0000 0.0005
323.15 0.0000 0.0003
323.15 0.0948 0.0003
323.15 0.1911 0.0003
323.15 0.2880 0.0003
323.15 0.3865 0.0003
323.15 0.4856 0.0004
323.15 0.5861 0.0004
323.15 0.6877 0.0004
323.15 0.7906 0.0004
323.15 0.8949 0.0004
323.15 1.0000 0.0005
333.15 0.0000 0.0003
333.15 0.0948 0.0003
333.15 0.1911 0.0003
333.15 0.2880 0.0003
333.15 0.3865 0.0003
333.15 0.4856 0.0003
333.15 0.5861 0.0003
333.15 0.6877 0.0004
333.15 0.7906 0.0004
333.15 0.8949 0.0004
333.15 1.0000 0.0004
343.15 0.0000 0.0003
343.15 0.0948 0.0003
343.15 0.1911 0.0003
343.15 0.2880 0.0003
343.15 0.3865 0.0003
343.15 0.4856 0.0003
343.15 0.5861 0.0003
343.15 0.6877 0.0003
343.15 0.7906 0.0003
343.15 0.8949 0.0003
343.15 1.0000 0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of p-Xylene (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0000 0.0004
298.15 0.0948 0.0004
298.15 0.1911 0.0004
298.15 0.2880 0.0004
298.15 0.3865 0.0004
298.15 0.4856 0.0005
298.15 0.5861 0.0005
298.15 0.6877 0.0005
298.15 0.7906 0.0005
298.15 0.8949 0.0006
298.15 1.0000 0.0006
303.15 0.0000 0.0004
303.15 0.0948 0.0004
303.15 0.1911 0.0004
303.15 0.2880 0.0004
303.15 0.3865 0.0004
303.15 0.4856 0.0004
303.15 0.5861 0.0004
303.15 0.6877 0.0005
303.15 0.7906 0.0005
303.15 0.8949 0.0005
303.15 1.0000 0.0006
313.15 0.0000 0.0003
313.15 0.0948 0.0003
313.15 0.1911 0.0004
313.15 0.2880 0.0004
313.15 0.3865 0.0004
313.15 0.4856 0.0004
313.15 0.5861 0.0004
313.15 0.6877 0.0004
313.15 0.7906 0.0004
313.15 0.8949 0.0005
313.15 1.0000 0.0005
323.15 0.0000 0.0003
323.15 0.0948 0.0003
323.15 0.1911 0.0003
323.15 0.2880 0.0003
323.15 0.3865 0.0003
323.15 0.4856 0.0004
323.15 0.5861 0.0004
323.15 0.6877 0.0004
323.15 0.7906 0.0004
323.15 0.8949 0.0004
323.15 1.0000 0.0005
333.15 0.0000 0.0003
333.15 0.0948 0.0003
333.15 0.1911 0.0003
333.15 0.2880 0.0003
333.15 0.3865 0.0003
333.15 0.4856 0.0003
333.15 0.5861 0.0003
333.15 0.6877 0.0004
333.15 0.7906 0.0004
333.15 0.8949 0.0004
333.15 1.0000 0.0004
343.15 0.0000 0.0003
343.15 0.0948 0.0003
343.15 0.1911 0.0003
343.15 0.2880 0.0003
343.15 0.3865 0.0003
343.15 0.4856 0.0003
343.15 0.5861 0.0003
343.15 0.6877 0.0003
343.15 0.7906 0.0003
343.15 0.8949 0.0003
343.15 1.0000 0.0004

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Heptane (2) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.1795 323.20 7.60
0.3708 323.20 10.40
0.5793 323.20 13.20
0.7845 323.20 15.70
0.1891 343.20 17.30
0.3689 343.20 22.60
0.5757 343.20 29.40
0.7734 343.20 34.70
0.1856 363.20 36.20
0.3568 363.20 45.10
0.5749 363.20 55.40
0.7694 363.20 64.90

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Mole fraction of Heptane (2) - Liquid Temperature, K - Liquid Vapor or sublimation pressure, kPa - Liquid
0.1795 323.20 7.60
0.3708 323.20 10.40
0.5793 323.20 13.20
0.7845 323.20 15.70
0.1891 343.20 17.30
0.3689 343.20 22.60
0.5757 343.20 29.40
0.7734 343.20 34.70
0.1856 363.20 36.20
0.3568 363.20 45.10
0.5749 363.20 55.40
0.7694 363.20 64.90

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of p-Xylene (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 679.9
298.15 0.0948 694.32
298.15 0.1911 709.39
298.15 0.2880 725.04
298.15 0.3865 741.5
298.15 0.4856 758.54
298.15 0.5861 776.51
298.15 0.6877 795.16
298.15 0.7906 814.74
298.15 0.8949 835.24
298.15 1.0000 856.7
303.15 0.0000 675.65
303.15 0.0948 690.05
303.15 0.1911 705.12
303.15 0.2880 720.75
303.15 0.3865 737.2
303.15 0.4856 754.24
303.15 0.5861 772.19
303.15 0.6877 790.83
303.15 0.7906 810.42
303.15 0.8949 830.91
303.15 1.0000 852.35
313.15 0.0000 667.08
313.15 0.0948 681.45
313.15 0.1911 696.52
313.15 0.2880 712.12
313.15 0.3865 728.57
313.15 0.4856 745.57
313.15 0.5861 763.52
313.15 0.6877 782.15
313.15 0.7906 801.71
313.15 0.8949 822.21
313.15 1.0000 843.64
323.15 0.0000 658.37
323.15 0.0948 672.73
323.15 0.1911 687.79
323.15 0.2880 703.38
323.15 0.3865 719.83
323.15 0.4856 736.82
323.15 0.5861 754.77
323.15 0.6877 773.41
323.15 0.7906 792.97
323.15 0.8949 813.45
323.15 1.0000 834.9
333.15 0.0000 649.53
333.15 0.0948 663.88
333.15 0.1911 678.95
333.15 0.2880 694.52
333.15 0.3865 710.98
333.15 0.4856 727.97
333.15 0.5861 745.92
333.15 0.6877 764.57
333.15 0.7906 784.15
333.15 0.8949 804.64
333.15 1.0000 826.09
343.15 0.0000 640.47
343.15 0.0948 654.83
343.15 0.1911 669.89
343.15 0.2880 685.48
343.15 0.3865 701.94
343.15 0.4856 718.94
343.15 0.5861 736.91
343.15 0.6877 755.57
343.15 0.7906 775.17
343.15 0.8949 795.69
343.15 1.0000 817.17

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of p-Xylene (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 679.9
298.15 0.0948 694.32
298.15 0.1911 709.39
298.15 0.2880 725.04
298.15 0.3865 741.5
298.15 0.4856 758.54
298.15 0.5861 776.51
298.15 0.6877 795.16
298.15 0.7906 814.74
298.15 0.8949 835.24
298.15 1.0000 856.7
303.15 0.0000 675.65
303.15 0.0948 690.05
303.15 0.1911 705.12
303.15 0.2880 720.75
303.15 0.3865 737.2
303.15 0.4856 754.24
303.15 0.5861 772.19
303.15 0.6877 790.83
303.15 0.7906 810.42
303.15 0.8949 830.91
303.15 1.0000 852.35
313.15 0.0000 667.08
313.15 0.0948 681.45
313.15 0.1911 696.52
313.15 0.2880 712.12
313.15 0.3865 728.57
313.15 0.4856 745.57
313.15 0.5861 763.52
313.15 0.6877 782.15
313.15 0.7906 801.71
313.15 0.8949 822.21
313.15 1.0000 843.64
323.15 0.0000 658.37
323.15 0.0948 672.73
323.15 0.1911 687.79
323.15 0.2880 703.38
323.15 0.3865 719.83
323.15 0.4856 736.82
323.15 0.5861 754.77
323.15 0.6877 773.41
323.15 0.7906 792.97
323.15 0.8949 813.45
323.15 1.0000 834.9
333.15 0.0000 649.53
333.15 0.0948 663.88
333.15 0.1911 678.95
333.15 0.2880 694.52
333.15 0.3865 710.98
333.15 0.4856 727.97
333.15 0.5861 745.92
333.15 0.6877 764.57
333.15 0.7906 784.15
333.15 0.8949 804.64
333.15 1.0000 826.09
343.15 0.0000 640.47
343.15 0.0948 654.83
343.15 0.1911 669.89
343.15 0.2880 685.48
343.15 0.3865 701.94
343.15 0.4856 718.94
343.15 0.5861 736.91
343.15 0.6877 755.57
343.15 0.7906 775.17
343.15 0.8949 795.69
343.15 1.0000 817.17

Sources