Mixture of 1-Hexanol + o-Xylene

Excel

1-Hexanol

Name
1-Hexanol
InChI
InChI=1S/C6H14O/c1-2-3-4-5-6-7/h7H,2-6H2,1H3
InChI Key
ZSIAUFGUXNUGDI-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CCCCCCO
Mol. Weight (g/mol)
102.17
CAS
111-27-3

o-Xylene

Name
o-Xylene
InChI
InChI=1S/C8H10/c1-7-5-3-4-6-8(7)2/h3-6H,1-2H3
InChI Key
CTQNGGLPUBDAKN-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1ccccc1C
Mol. Weight (g/mol)
106.17
CAS
95-47-6
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Datasets

  1. Mole fraction (2)
  2. η - Viscosity, Pa*s (2)
  3. ρl - Mass density, kg/m3 (2)
  4. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of o-Xylene (2) [ref]

Fixed Measured
Mole fraction of o-Xylene (2) - Liquid Temperature, K - Liquid Mole fraction of o-Xylene (2) - Gas
0.0000 428.45 0.0000
0.0625 427.45 0.0948
0.1035 426.75 0.1540
0.1800 425.45 0.2583
0.2597 424.15 0.3585
0.3192 423.15 0.4279
0.3654 422.45 0.4787
0.4279 421.45 0.5434
0.4795 420.65 0.5934
0.5560 419.55 0.6623
0.6500 418.35 0.7392
0.7111 417.65 0.7854
0.8233 416.55 0.8650
0.8858 416.05 0.9087
0.9350 415.75 0.9449
1.0000 415.45 1.0000

Mole fraction of o-Xylene (2) [ref]

Fixed Measured
Mole fraction of o-Xylene (2) - Liquid Temperature, K - Liquid Mole fraction of o-Xylene (2) - Gas
0.0000 428.45 0.0000
0.0625 427.45 0.0948
0.1035 426.75 0.1540
0.1800 425.45 0.2583
0.2597 424.15 0.3585
0.3192 423.15 0.4279
0.3654 422.45 0.4787
0.4279 421.45 0.5434
0.4795 420.65 0.5934
0.5560 419.55 0.6623
0.6500 418.35 0.7392
0.7111 417.65 0.7854
0.8233 416.55 0.8650
0.8858 416.05 0.9087
0.9350 415.75 0.9449
1.0000 415.45 1.0000

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Hexanol (1) - Liquid Viscosity, Pa*s - Liquid
308.15 0.0000 0.0007
308.15 0.0999 0.0007
308.15 0.1999 0.0008
308.15 0.2999 0.0009
308.15 0.4001 0.0010
308.15 0.4997 0.0012
308.15 0.6000 0.0015
308.15 0.7000 0.0018
308.15 0.8000 0.0022
308.15 0.8999 0.0027
308.15 1.0000 0.0033
318.15 0.0000 0.0006
318.15 0.0999 0.0006
318.15 0.1999 0.0007
318.15 0.2999 0.0008
318.15 0.4001 0.0009
318.15 0.4997 0.0010
318.15 0.6000 0.0012
318.15 0.7000 0.0014
318.15 0.8000 0.0017
318.15 0.8999 0.0021
318.15 1.0000 0.0025

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Hexanol (1) - Liquid Viscosity, Pa*s - Liquid
308.15 0.0000 0.0007
308.15 0.0999 0.0007
308.15 0.1999 0.0008
308.15 0.2999 0.0009
308.15 0.4001 0.0010
308.15 0.4997 0.0012
308.15 0.6000 0.0015
308.15 0.7000 0.0018
308.15 0.8000 0.0022
308.15 0.8999 0.0027
308.15 1.0000 0.0033
318.15 0.0000 0.0006
318.15 0.0999 0.0006
318.15 0.1999 0.0007
318.15 0.2999 0.0008
318.15 0.4001 0.0009
318.15 0.4997 0.0010
318.15 0.6000 0.0012
318.15 0.7000 0.0014
318.15 0.8000 0.0017
318.15 0.8999 0.0021
318.15 1.0000 0.0025

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Hexanol (1) - Liquid Mass density, kg/m3 - Liquid
308.15 0.0000 866.7
308.15 0.0999 860.1
308.15 0.1999 853.9
308.15 0.2999 847.9
308.15 0.4001 842.1
308.15 0.4997 836.4
308.15 0.6000 830.7
308.15 0.7000 825.1
308.15 0.8000 819.5
308.15 0.8999 814.0
308.15 1.0000 808.5
318.15 0.0000 858.4
318.15 0.0999 851.7
318.15 0.1999 845.6
318.15 0.2999 839.7
318.15 0.4001 833.9
318.15 0.4997 828.3
318.15 0.6000 822.7
318.15 0.7000 817.2
318.15 0.8000 811.8
318.15 0.8999 806.4
318.15 1.0000 801.2

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Hexanol (1) - Liquid Mass density, kg/m3 - Liquid
308.15 0.0000 866.7
308.15 0.0999 860.1
308.15 0.1999 853.9
308.15 0.2999 847.9
308.15 0.4001 842.1
308.15 0.4997 836.4
308.15 0.6000 830.7
308.15 0.7000 825.1
308.15 0.8000 819.5
308.15 0.8999 814.0
308.15 1.0000 808.5
318.15 0.0000 858.4
318.15 0.0999 851.7
318.15 0.1999 845.6
318.15 0.2999 839.7
318.15 0.4001 833.9
318.15 0.4997 828.3
318.15 0.6000 822.7
318.15 0.7000 817.2
318.15 0.8000 811.8
318.15 0.8999 806.4
318.15 1.0000 801.2

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.6 (Liquid)

Mole fraction of o-Xylene (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 428.45
0.0625 427.45
0.1035 426.75
0.1800 425.45
0.2597 424.15
0.3192 423.15
0.3654 422.45
0.4279 421.45
0.4795 420.65
0.5560 419.55
0.6500 418.35
0.7111 417.65
0.8233 416.55
0.8858 416.05
0.9350 415.75
1.0000 415.45

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.6 (Liquid)

Mole fraction of o-Xylene (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 428.45
0.0625 427.45
0.1035 426.75
0.1800 425.45
0.2597 424.15
0.3192 423.15
0.3654 422.45
0.4279 421.45
0.4795 420.65
0.5560 419.55
0.6500 418.35
0.7111 417.65
0.8233 416.55
0.8858 416.05
0.9350 415.75
1.0000 415.45

Sources