Mixture of Benzene + Cyclohexanone

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

Cyclohexanone

Name
Cyclohexanone
InChI
InChI=1S/C6H10O/c7-6-4-2-1-3-5-6/h1-5H2
InChI Key
JHIVVAPYMSGYDF-UHFFFAOYSA-N
Formula
C6H10O
SMILES
O=C1CCCCC1
Mol. Weight (g/mol)
98.14
CAS
108-94-1
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. Mole fraction (2)
  2. Tboil - Boiling temperature at pressure P, K (2)
  3. Excess molar volume, m3/mol (2)

Mole fraction of Cyclohexanone (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Cyclohexanone (2) - Liquid Mole fraction of Cyclohexanone (2) - Gas
0.1106 0.0115
0.2438 0.0249
0.3124 0.0360
0.4155 0.0573
0.5260 0.0930
0.6064 0.1324
0.6841 0.1904
0.7385 0.2459
0.7966 0.3365
0.8339 0.4131
0.8652 0.4877
0.8979 0.5849
0.9396 0.7368
0.9682 0.8621

Mole fraction of Cyclohexanone (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Cyclohexanone (2) - Liquid Mole fraction of Cyclohexanone (2) - Gas
0.1106 0.0115
0.2438 0.0249
0.3124 0.0360
0.4155 0.0573
0.5260 0.0930
0.6064 0.1324
0.6841 0.1904
0.7385 0.2459
0.7966 0.3365
0.8339 0.4131
0.8652 0.4877
0.8979 0.5849
0.9396 0.7368
0.9682 0.8621

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Cyclohexanone (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.1106 356.30
0.2438 360.15
0.3124 362.65
0.4155 367.25
0.5260 373.60
0.6064 379.50
0.6841 386.40
0.7385 391.90
0.7966 398.90
0.8339 403.85
0.8652 408.20
0.8979 412.90
0.9396 419.25
0.9682 423.75

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Cyclohexanone (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.1106 356.30
0.2438 360.15
0.3124 362.65
0.4155 367.25
0.5260 373.60
0.6064 379.50
0.6841 386.40
0.7385 391.90
0.7966 398.90
0.8339 403.85
0.8652 408.20
0.8979 412.90
0.9396 419.25
0.9682 423.75

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Benzene (1) - Liquid Excess molar volume, m3/mol - Liquid
298.15 0.0790 -5.7400e-08
298.15 0.1856 -1.1570e-07
298.15 0.2569 -1.4850e-07
298.15 0.3695 -1.8950e-07
298.15 0.4589 -2.1260e-07
298.15 0.4965 -2.2080e-07
298.15 0.5201 -2.2410e-07
298.15 0.5623 -2.2810e-07
298.15 0.6589 -2.2450e-07
298.15 0.7001 -2.1500e-07
298.15 0.7258 -2.0770e-07
298.15 0.8003 -1.7570e-07
298.15 0.8665 -1.3290e-07
298.15 0.9214 -8.6600e-08
303.15 0.0786 -4.9700e-08
303.15 0.1754 -9.6900e-08
303.15 0.2569 -1.2970e-07
303.15 0.3598 -1.6370e-07
303.15 0.4372 -1.8450e-07
303.15 0.4556 -1.8790e-07
303.15 0.4859 -1.9370e-07
303.15 0.5263 -1.9900e-07
303.15 0.5896 -2.0210e-07
303.15 0.6258 -2.0500e-07
303.15 0.7589 -1.7720e-07
303.15 0.8520 -1.3170e-07
303.15 0.8965 -9.9200e-08
303.15 0.9458 -5.6100e-08
313.15 0.0786 -4.3100e-08
313.15 0.1374 -6.8500e-08
313.15 0.2437 -1.0630e-07
313.15 0.3714 -1.4210e-07
313.15 0.4137 -1.5320e-07
313.15 0.4585 -1.6350e-07
313.15 0.5263 -1.7530e-07
313.15 0.6258 -1.8060e-07
313.15 0.6658 -1.7920e-07
313.15 0.7425 -1.6410e-07
313.15 0.7915 -1.4850e-07
313.15 0.8569 -1.1510e-07
313.15 0.9005 -8.7100e-08
313.15 0.9556 -4.2300e-08
323.15 0.0786 -3.5100e-08
323.15 0.1596 -6.3600e-08
323.15 0.2589 -9.0500e-08
323.15 0.3695 -1.2070e-07
323.15 0.3896 -1.2450e-07
323.15 0.4589 -1.3890e-07
323.15 0.4852 -1.4280e-07
323.15 0.5896 -1.5650e-07
323.15 0.6859 -1.5520e-07
323.15 0.7589 -1.4070e-07
323.15 0.7859 -1.3290e-07
323.15 0.8569 -1.0320e-07
323.15 0.8956 -8.1500e-08
323.15 0.9514 -4.2800e-08
333.15 0.0759 -2.7100e-08
333.15 0.1856 -5.5400e-08
333.15 0.2569 -7.2500e-08
333.15 0.3252 -8.5900e-08
333.15 0.3688 -9.5900e-08
333.15 0.4259 -1.0680e-07
333.15 0.4856 -1.1860e-07
333.15 0.5326 -1.2630e-07
333.15 0.6052 -1.3210e-07
333.15 0.6852 -1.3180e-07
333.15 0.7326 -1.2740e-07
333.15 0.7893 -1.1640e-07
333.15 0.8562 -9.2300e-08
333.15 0.9256 -5.4100e-08
343.15 0.0583 -1.5800e-08
343.15 0.1497 -3.4300e-08
343.15 0.2168 -4.5100e-08
343.15 0.2889 -5.9200e-08
343.15 0.3587 -7.0200e-08
343.15 0.4197 -8.2500e-08
343.15 0.4896 -9.4600e-08
343.15 0.5256 -1.0040e-07
343.15 0.5899 -1.0710e-07
343.15 0.6485 -1.1200e-07
343.15 0.7095 -1.1030e-07
343.15 0.7895 -9.9800e-08
343.15 0.8656 -7.6300e-08
343.15 0.9365 -4.0300e-08
353.15 0.0598 -1.2100e-08
353.15 0.1395 -2.1200e-08
353.15 0.2058 -2.8300e-08
353.15 0.2758 -3.6600e-08
353.15 0.3558 -4.7600e-08
353.15 0.4256 -5.9400e-08
353.15 0.4931 -7.0200e-08
353.15 0.5335 -7.6100e-08
353.15 0.6147 -8.5100e-08
353.15 0.6732 -8.8400e-08
353.15 0.7422 -8.8300e-08
353.15 0.8057 -8.0200e-08
353.15 0.8752 -6.0300e-08
353.15 0.9215 -4.2200e-08

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Benzene (1) - Liquid Excess molar volume, m3/mol - Liquid
298.15 0.0790 -5.7400e-08
298.15 0.1856 -1.1570e-07
298.15 0.2569 -1.4850e-07
298.15 0.3695 -1.8950e-07
298.15 0.4589 -2.1260e-07
298.15 0.4965 -2.2080e-07
298.15 0.5201 -2.2410e-07
298.15 0.5623 -2.2810e-07
298.15 0.6589 -2.2450e-07
298.15 0.7001 -2.1500e-07
298.15 0.7258 -2.0770e-07
298.15 0.8003 -1.7570e-07
298.15 0.8665 -1.3290e-07
298.15 0.9214 -8.6600e-08
303.15 0.0786 -4.9700e-08
303.15 0.1754 -9.6900e-08
303.15 0.2569 -1.2970e-07
303.15 0.3598 -1.6370e-07
303.15 0.4372 -1.8450e-07
303.15 0.4556 -1.8790e-07
303.15 0.4859 -1.9370e-07
303.15 0.5263 -1.9900e-07
303.15 0.5896 -2.0210e-07
303.15 0.6258 -2.0500e-07
303.15 0.7589 -1.7720e-07
303.15 0.8520 -1.3170e-07
303.15 0.8965 -9.9200e-08
303.15 0.9458 -5.6100e-08
313.15 0.0786 -4.3100e-08
313.15 0.1374 -6.8500e-08
313.15 0.2437 -1.0630e-07
313.15 0.3714 -1.4210e-07
313.15 0.4137 -1.5320e-07
313.15 0.4585 -1.6350e-07
313.15 0.5263 -1.7530e-07
313.15 0.6258 -1.8060e-07
313.15 0.6658 -1.7920e-07
313.15 0.7425 -1.6410e-07
313.15 0.7915 -1.4850e-07
313.15 0.8569 -1.1510e-07
313.15 0.9005 -8.7100e-08
313.15 0.9556 -4.2300e-08
323.15 0.0786 -3.5100e-08
323.15 0.1596 -6.3600e-08
323.15 0.2589 -9.0500e-08
323.15 0.3695 -1.2070e-07
323.15 0.3896 -1.2450e-07
323.15 0.4589 -1.3890e-07
323.15 0.4852 -1.4280e-07
323.15 0.5896 -1.5650e-07
323.15 0.6859 -1.5520e-07
323.15 0.7589 -1.4070e-07
323.15 0.7859 -1.3290e-07
323.15 0.8569 -1.0320e-07
323.15 0.8956 -8.1500e-08
323.15 0.9514 -4.2800e-08
333.15 0.0759 -2.7100e-08
333.15 0.1856 -5.5400e-08
333.15 0.2569 -7.2500e-08
333.15 0.3252 -8.5900e-08
333.15 0.3688 -9.5900e-08
333.15 0.4259 -1.0680e-07
333.15 0.4856 -1.1860e-07
333.15 0.5326 -1.2630e-07
333.15 0.6052 -1.3210e-07
333.15 0.6852 -1.3180e-07
333.15 0.7326 -1.2740e-07
333.15 0.7893 -1.1640e-07
333.15 0.8562 -9.2300e-08
333.15 0.9256 -5.4100e-08
343.15 0.0583 -1.5800e-08
343.15 0.1497 -3.4300e-08
343.15 0.2168 -4.5100e-08
343.15 0.2889 -5.9200e-08
343.15 0.3587 -7.0200e-08
343.15 0.4197 -8.2500e-08
343.15 0.4896 -9.4600e-08
343.15 0.5256 -1.0040e-07
343.15 0.5899 -1.0710e-07
343.15 0.6485 -1.1200e-07
343.15 0.7095 -1.1030e-07
343.15 0.7895 -9.9800e-08
343.15 0.8656 -7.6300e-08
343.15 0.9365 -4.0300e-08
353.15 0.0598 -1.2100e-08
353.15 0.1395 -2.1200e-08
353.15 0.2058 -2.8300e-08
353.15 0.2758 -3.6600e-08
353.15 0.3558 -4.7600e-08
353.15 0.4256 -5.9400e-08
353.15 0.4931 -7.0200e-08
353.15 0.5335 -7.6100e-08
353.15 0.6147 -8.5100e-08
353.15 0.6732 -8.8400e-08
353.15 0.7422 -8.8300e-08
353.15 0.8057 -8.0200e-08
353.15 0.8752 -6.0300e-08
353.15 0.9215 -4.2200e-08

Sources