Mixture of 2-Butanone + 2-Pentanol

Excel

2-Butanone

Name
2-Butanone
InChI
InChI=1S/C4H8O/c1-3-4(2)5/h3H2,1-2H3
InChI Key
ZWEHNKRNPOVVGH-UHFFFAOYSA-N
Formula
C4H8O
SMILES
CCC(C)=O
Mol. Weight (g/mol)
72.11
CAS
78-93-3

2-Pentanol

Name
2-Pentanol
InChI
InChI=1S/C5H12O/c1-3-4-5(2)6/h5-6H,3-4H2,1-2H3
InChI Key
JYVLIDXNZAXMDK-UHFFFAOYSA-N
Formula
C5H12O
SMILES
CCCC(C)O
Mol. Weight (g/mol)
88.15
CAS
6032-29-7
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Datasets

  1. η - Viscosity, Pa*s (4)
  2. n0 - Refractive index (Na D-line) (2)
  3. ρl - Mass density, kg/m3 (4)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0000 0.0035
298.15 0.0852 0.0025
298.15 0.1643 0.0020
298.15 0.2456 0.0016
298.15 0.3511 0.0012
298.15 0.4422 0.0009
298.15 0.5632 0.0007
298.15 0.6508 0.0006
298.15 0.7416 0.0006
298.15 0.8512 0.0005
298.15 0.9410 0.0004
298.15 1.0000 0.0004
303.15 0.0000 0.0028
303.15 0.0852 0.0022
303.15 0.1643 0.0018
303.15 0.2456 0.0014
303.15 0.3511 0.0011
303.15 0.4422 0.0009
303.15 0.5632 0.0007
303.15 0.6508 0.0006
303.15 0.7416 0.0005
303.15 0.8512 0.0005
303.15 0.9410 0.0004
303.15 1.0000 0.0004
308.15 0.0000 0.0023
308.15 0.0852 0.0019
308.15 0.1643 0.0016
308.15 0.2456 0.0013
308.15 0.3511 0.0010
308.15 0.4422 0.0009
308.15 0.5632 0.0007
308.15 0.6508 0.0006
308.15 0.7416 0.0005
308.15 0.8512 0.0004
308.15 0.9410 0.0004
308.15 1.0000 0.0004
313.15 0.0000 0.0020
313.15 0.0852 0.0017
313.15 0.1643 0.0014
313.15 0.2456 0.0012
313.15 0.3511 0.0010
313.15 0.4422 0.0008
313.15 0.5632 0.0007
313.15 0.6508 0.0006
313.15 0.7416 0.0005
313.15 0.8512 0.0004
313.15 0.9410 0.0004
313.15 1.0000 0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0000 0.0035
298.15 0.0824 0.0027
298.15 0.1612 0.0021
298.15 0.2401 0.0017
298.15 0.3519 0.0013
298.15 0.4396 0.0011
298.15 0.5608 0.0009
298.15 0.6494 0.0007
298.15 0.7403 0.0006
298.15 0.8491 0.0005
298.15 0.9384 0.0004
298.15 1.0000 0.0004
308.15 0.0000 0.0024
308.15 0.0824 0.0018
308.15 0.1612 0.0014
308.15 0.2401 0.0011
308.15 0.3519 0.0009
308.15 0.4396 0.0007
308.15 0.5608 0.0006
308.15 0.6494 0.0005
308.15 0.7403 0.0005
308.15 0.8491 0.0004
308.15 0.9384 0.0004
308.15 1.0000 0.0004
318.15 0.0000 0.0018
318.15 0.0824 0.0013
318.15 0.1612 0.0011
318.15 0.2401 0.0009
318.15 0.3519 0.0007
318.15 0.4396 0.0006
318.15 0.5608 0.0005
318.15 0.6494 0.0005
318.15 0.7403 0.0004
318.15 0.8491 0.0004
318.15 0.9384 0.0003
318.15 1.0000 0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0000 0.0035
298.15 0.0852 0.0025
298.15 0.1643 0.0020
298.15 0.2456 0.0016
298.15 0.3511 0.0012
298.15 0.4422 0.0009
298.15 0.5632 0.0007
298.15 0.6508 0.0006
298.15 0.7416 0.0006
298.15 0.8512 0.0005
298.15 0.9410 0.0004
298.15 1.0000 0.0004
303.15 0.0000 0.0028
303.15 0.0852 0.0022
303.15 0.1643 0.0018
303.15 0.2456 0.0014
303.15 0.3511 0.0011
303.15 0.4422 0.0009
303.15 0.5632 0.0007
303.15 0.6508 0.0006
303.15 0.7416 0.0005
303.15 0.8512 0.0005
303.15 0.9410 0.0004
303.15 1.0000 0.0004
308.15 0.0000 0.0023
308.15 0.0852 0.0019
308.15 0.1643 0.0016
308.15 0.2456 0.0013
308.15 0.3511 0.0010
308.15 0.4422 0.0009
308.15 0.5632 0.0007
308.15 0.6508 0.0006
308.15 0.7416 0.0005
308.15 0.8512 0.0004
308.15 0.9410 0.0004
308.15 1.0000 0.0004
313.15 0.0000 0.0020
313.15 0.0852 0.0017
313.15 0.1643 0.0014
313.15 0.2456 0.0012
313.15 0.3511 0.0010
313.15 0.4422 0.0008
313.15 0.5632 0.0007
313.15 0.6508 0.0006
313.15 0.7416 0.0005
313.15 0.8512 0.0004
313.15 0.9410 0.0004
313.15 1.0000 0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0000 0.0035
298.15 0.0824 0.0027
298.15 0.1612 0.0021
298.15 0.2401 0.0017
298.15 0.3519 0.0013
298.15 0.4396 0.0011
298.15 0.5608 0.0009
298.15 0.6494 0.0007
298.15 0.7403 0.0006
298.15 0.8491 0.0005
298.15 0.9384 0.0004
298.15 1.0000 0.0004
308.15 0.0000 0.0024
308.15 0.0824 0.0018
308.15 0.1612 0.0014
308.15 0.2401 0.0011
308.15 0.3519 0.0009
308.15 0.4396 0.0007
308.15 0.5608 0.0006
308.15 0.6494 0.0005
308.15 0.7403 0.0005
308.15 0.8491 0.0004
308.15 0.9384 0.0004
308.15 1.0000 0.0004
318.15 0.0000 0.0018
318.15 0.0824 0.0013
318.15 0.1612 0.0011
318.15 0.2401 0.0009
318.15 0.3519 0.0007
318.15 0.4396 0.0006
318.15 0.5608 0.0005
318.15 0.6494 0.0005
318.15 0.7403 0.0004
318.15 0.8491 0.0004
318.15 0.9384 0.0003
318.15 1.0000 0.0003

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (1) - Liquid Refractive index (Na D-line) - Liquid
298.15 0.0000 1.4032
298.15 0.0824 1.4014
298.15 0.1612 1.3998
298.15 0.2401 1.398
298.15 0.3519 1.3952
298.15 0.4396 1.3929
298.15 0.5608 1.3895
298.15 0.6494 1.3868
298.15 0.7403 1.384
298.15 0.8491 1.3803
298.15 0.9384 1.3772
298.15 1.0000 1.375
308.15 0.0000 1.399
308.15 0.0824 1.3974
308.15 0.1612 1.3959
308.15 0.2401 1.3941
308.15 0.3519 1.3914
308.15 0.4396 1.389
308.15 0.5608 1.3854
308.15 0.6494 1.3826
308.15 0.7403 1.3796
308.15 0.8491 1.3757
308.15 0.9384 1.3724
308.15 1.0000 1.37
318.15 0.0000 1.395
318.15 0.0824 1.3937
318.15 0.1612 1.3923
318.15 0.2401 1.3906
318.15 0.3519 1.3877
318.15 0.4396 1.3852
318.15 0.5608 1.3813
318.15 0.6494 1.3782
318.15 0.7403 1.375
318.15 0.8491 1.3711
318.15 0.9384 1.3679
318.15 1.0000 1.3657

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (1) - Liquid Refractive index (Na D-line) - Liquid
298.15 0.0000 1.4032
298.15 0.0824 1.4014
298.15 0.1612 1.3998
298.15 0.2401 1.398
298.15 0.3519 1.3952
298.15 0.4396 1.3929
298.15 0.5608 1.3895
298.15 0.6494 1.3868
298.15 0.7403 1.384
298.15 0.8491 1.3803
298.15 0.9384 1.3772
298.15 1.0000 1.375
308.15 0.0000 1.399
308.15 0.0824 1.3974
308.15 0.1612 1.3959
308.15 0.2401 1.3941
308.15 0.3519 1.3914
308.15 0.4396 1.389
308.15 0.5608 1.3854
308.15 0.6494 1.3826
308.15 0.7403 1.3796
308.15 0.8491 1.3757
308.15 0.9384 1.3724
308.15 1.0000 1.37
318.15 0.0000 1.395
318.15 0.0824 1.3937
318.15 0.1612 1.3923
318.15 0.2401 1.3906
318.15 0.3519 1.3877
318.15 0.4396 1.3852
318.15 0.5608 1.3813
318.15 0.6494 1.3782
318.15 0.7403 1.375
318.15 0.8491 1.3711
318.15 0.9384 1.3679
318.15 1.0000 1.3657

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 805.41
298.15 0.0852 804.2
298.15 0.1643 803.1
298.15 0.2456 802.1
298.15 0.3511 801.0
298.15 0.4422 800.24
298.15 0.5632 799.6
298.15 0.6508 799.3
298.15 0.7416 799.14
298.15 0.8512 799.2
298.15 0.9410 799.31
298.15 1.0000 799.48
303.15 0.0000 801.21
303.15 0.0852 799.84
303.15 0.1643 798.76
303.15 0.2456 797.76
303.15 0.3511 796.62
303.15 0.4422 795.77
303.15 0.5632 794.94
303.15 0.6508 794.56
303.15 0.7416 794.34
303.15 0.8512 794.26
303.15 0.9410 794.39
303.15 1.0000 794.63
308.15 0.0000 796.64
308.15 0.0852 795.37
308.15 0.1643 794.25
308.15 0.2456 793.2
308.15 0.3511 791.97
308.15 0.4422 791.11
308.15 0.5632 790.27
308.15 0.6508 789.87
308.15 0.7416 789.63
308.15 0.8512 789.56
308.15 0.9410 789.76
308.15 1.0000 789.9
313.15 0.0000 792.51
313.15 0.0852 791.21
313.15 0.1643 790.05
313.15 0.2456 788.94
313.15 0.3511 787.7
313.15 0.4422 786.83
313.15 0.5632 785.94
313.15 0.6508 785.47
313.15 0.7416 785.18
313.15 0.8512 785.05
313.15 0.9410 785.17
313.15 1.0000 785.52

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 805.3
298.15 0.0824 804.0
298.15 0.1612 802.99
298.15 0.2401 802.04
298.15 0.3519 800.97
298.15 0.4396 800.31
298.15 0.5608 799.65
298.15 0.6494 799.34
298.15 0.7403 799.2
298.15 0.8491 799.26
298.15 0.9384 799.49
298.15 1.0000 799.76
308.15 0.0000 797.0
308.15 0.0824 795.54
308.15 0.1612 794.34
308.15 0.2401 793.29
308.15 0.3519 791.97
308.15 0.4396 791.07
308.15 0.5608 790.15
308.15 0.6494 789.63
308.15 0.7403 789.23
308.15 0.8491 789.02
308.15 0.9384 789.09
308.15 1.0000 789.21
318.15 0.0000 788.37
318.15 0.0824 786.83
318.15 0.1612 785.5
318.15 0.2401 784.32
318.15 0.3519 782.76
318.15 0.4396 781.66
318.15 0.5608 780.47
318.15 0.6494 779.91
318.15 0.7403 779.15
318.15 0.8491 778.67
318.15 0.9384 778.55
318.15 1.0000 778.52

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 805.41
298.15 0.0852 804.2
298.15 0.1643 803.1
298.15 0.2456 802.1
298.15 0.3511 801.0
298.15 0.4422 800.24
298.15 0.5632 799.6
298.15 0.6508 799.3
298.15 0.7416 799.14
298.15 0.8512 799.2
298.15 0.9410 799.31
298.15 1.0000 799.48
303.15 0.0000 801.21
303.15 0.0852 799.84
303.15 0.1643 798.76
303.15 0.2456 797.76
303.15 0.3511 796.62
303.15 0.4422 795.77
303.15 0.5632 794.94
303.15 0.6508 794.56
303.15 0.7416 794.34
303.15 0.8512 794.26
303.15 0.9410 794.39
303.15 1.0000 794.63
308.15 0.0000 796.64
308.15 0.0852 795.37
308.15 0.1643 794.25
308.15 0.2456 793.2
308.15 0.3511 791.97
308.15 0.4422 791.11
308.15 0.5632 790.27
308.15 0.6508 789.87
308.15 0.7416 789.63
308.15 0.8512 789.56
308.15 0.9410 789.76
308.15 1.0000 789.9
313.15 0.0000 792.51
313.15 0.0852 791.21
313.15 0.1643 790.05
313.15 0.2456 788.94
313.15 0.3511 787.7
313.15 0.4422 786.83
313.15 0.5632 785.94
313.15 0.6508 785.47
313.15 0.7416 785.18
313.15 0.8512 785.05
313.15 0.9410 785.17
313.15 1.0000 785.52

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 805.3
298.15 0.0824 804.0
298.15 0.1612 802.99
298.15 0.2401 802.04
298.15 0.3519 800.97
298.15 0.4396 800.31
298.15 0.5608 799.65
298.15 0.6494 799.34
298.15 0.7403 799.2
298.15 0.8491 799.26
298.15 0.9384 799.49
298.15 1.0000 799.76
308.15 0.0000 797.0
308.15 0.0824 795.54
308.15 0.1612 794.34
308.15 0.2401 793.29
308.15 0.3519 791.97
308.15 0.4396 791.07
308.15 0.5608 790.15
308.15 0.6494 789.63
308.15 0.7403 789.23
308.15 0.8491 789.02
308.15 0.9384 789.09
308.15 1.0000 789.21
318.15 0.0000 788.37
318.15 0.0824 786.83
318.15 0.1612 785.5
318.15 0.2401 784.32
318.15 0.3519 782.76
318.15 0.4396 781.66
318.15 0.5608 780.47
318.15 0.6494 779.91
318.15 0.7403 779.15
318.15 0.8491 778.67
318.15 0.9384 778.55
318.15 1.0000 778.52

Sources