Mixture of Benzene + 2-Butanone

Excel

Benzene

Name
Benzene
InChI
InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H
InChI Key
UHOVQNZJYSORNB-UHFFFAOYSA-N
Formula
C6H6
SMILES
c1ccccc1
Mol. Weight (g/mol)
78.11
CAS
71-43-2

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
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

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

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (2) - Liquid Viscosity, Pa*s - Liquid
303.15 0.0000 0.0006
303.15 0.1010 0.0005
303.15 0.1999 0.0005
303.15 0.2988 0.0005
303.15 0.3969 0.0005
303.15 0.4996 0.0004
303.15 0.5988 0.0004
303.15 0.6993 0.0004
303.15 0.7931 0.0004
303.15 0.8961 0.0004
303.15 1.0000 0.0004
313.15 0.0000 0.0005
313.15 0.1010 0.0005
313.15 0.1999 0.0004
313.15 0.2988 0.0004
313.15 0.3969 0.0004
313.15 0.4996 0.0004
313.15 0.5988 0.0004
313.15 0.6993 0.0004
313.15 0.7931 0.0004
313.15 0.8961 0.0003
313.15 1.0000 0.0003
323.15 0.0000 0.0004
323.15 0.1010 0.0004
323.15 0.1999 0.0004
323.15 0.2988 0.0004
323.15 0.3969 0.0004
323.15 0.4996 0.0004
323.15 0.5988 0.0003
323.15 0.6993 0.0003
323.15 0.7931 0.0003
323.15 0.8961 0.0003
323.15 1.0000 0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (2) - Liquid Viscosity, Pa*s - Liquid
303.15 0.0000 0.0006
303.15 0.1010 0.0005
303.15 0.1999 0.0005
303.15 0.2988 0.0005
303.15 0.3969 0.0005
303.15 0.4996 0.0004
303.15 0.5988 0.0004
303.15 0.6993 0.0004
303.15 0.7931 0.0004
303.15 0.8961 0.0004
303.15 1.0000 0.0004
313.15 0.0000 0.0005
313.15 0.1010 0.0005
313.15 0.1999 0.0004
313.15 0.2988 0.0004
313.15 0.3969 0.0004
313.15 0.4996 0.0004
313.15 0.5988 0.0004
313.15 0.6993 0.0004
313.15 0.7931 0.0004
313.15 0.8961 0.0003
313.15 1.0000 0.0003
323.15 0.0000 0.0004
323.15 0.1010 0.0004
323.15 0.1999 0.0004
323.15 0.2988 0.0004
323.15 0.3969 0.0004
323.15 0.4996 0.0004
323.15 0.5988 0.0003
323.15 0.6993 0.0003
323.15 0.7931 0.0003
323.15 0.8961 0.0003
323.15 1.0000 0.0003

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (2) - Liquid Mass density, kg/m3 - Liquid
303.15 0.0000 868.1
303.15 0.1010 861.2
303.15 0.1999 854.2
303.15 0.2988 847.1
303.15 0.3969 839.9
303.15 0.4996 832.7
303.15 0.5988 825.2
303.15 0.6993 817.5
303.15 0.7931 809.9
303.15 0.8961 802.2
303.15 1.0000 794.6
313.15 0.0000 857.4
313.15 0.1010 850.6
313.15 0.1999 843.5
313.15 0.2988 836.6
313.15 0.3969 829.3
313.15 0.4996 822.1
313.15 0.5988 814.6
313.15 0.6993 806.9
313.15 0.7931 799.4
313.15 0.8961 791.7
313.15 1.0000 784.0
323.15 0.0000 846.6
323.15 0.1010 839.9
323.15 0.1999 832.9
323.15 0.2988 825.9
323.15 0.3969 818.7
323.15 0.4996 811.5
323.15 0.5988 803.9
323.15 0.6993 796.4
323.15 0.7931 788.9
323.15 0.8961 781.1
323.15 1.0000 773.3

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 2-Butanone (2) - Liquid Mass density, kg/m3 - Liquid
303.15 0.0000 868.1
303.15 0.1010 861.2
303.15 0.1999 854.2
303.15 0.2988 847.1
303.15 0.3969 839.9
303.15 0.4996 832.7
303.15 0.5988 825.2
303.15 0.6993 817.5
303.15 0.7931 809.9
303.15 0.8961 802.2
303.15 1.0000 794.6
313.15 0.0000 857.4
313.15 0.1010 850.6
313.15 0.1999 843.5
313.15 0.2988 836.6
313.15 0.3969 829.3
313.15 0.4996 822.1
313.15 0.5988 814.6
313.15 0.6993 806.9
313.15 0.7931 799.4
313.15 0.8961 791.7
313.15 1.0000 784.0
323.15 0.0000 846.6
323.15 0.1010 839.9
323.15 0.1999 832.9
323.15 0.2988 825.9
323.15 0.3969 818.7
323.15 0.4996 811.5
323.15 0.5988 803.9
323.15 0.6993 796.4
323.15 0.7931 788.9
323.15 0.8961 781.1
323.15 1.0000 773.3

Sources