Mixture of Toluene + Cyclohexanone

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Toluene

Name
Toluene
InChI
InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3
InChI Key
YXFVVABEGXRONW-UHFFFAOYSA-N
Formula
C7H8
SMILES
Cc1ccccc1
Mol. Weight (g/mol)
92.14
CAS
108-88-3

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
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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
0.0096 0.0048
0.0573 0.0224
0.1397 0.0458
0.2781 0.0898
0.4362 0.1589
0.5585 0.2411
0.5810 0.2625
0.6251 0.3032
0.6670 0.3500
0.7573 0.4662
0.8365 0.5967
0.8815 0.6860
0.9186 0.7710
0.9886 0.9638

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
0.0096 0.0048
0.0573 0.0224
0.1397 0.0458
0.2781 0.0898
0.4362 0.1589
0.5585 0.2411
0.5810 0.2625
0.6251 0.3032
0.6670 0.3500
0.7573 0.4662
0.8365 0.5967
0.8815 0.6860
0.9186 0.7710
0.9886 0.9638

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
0.0096 384.00
0.0573 384.85
0.1397 386.45
0.2781 389.55
0.4362 394.95
0.5585 400.25
0.5810 401.35
0.6251 403.55
0.6670 405.75
0.7573 410.95
0.8365 416.15
0.8815 419.25
0.9186 421.95
0.9886 427.55

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
0.0096 384.00
0.0573 384.85
0.1397 386.45
0.2781 389.55
0.4362 394.95
0.5585 400.25
0.5810 401.35
0.6251 403.55
0.6670 405.75
0.7573 410.95
0.8365 416.15
0.8815 419.25
0.9186 421.95
0.9886 427.55

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Toluene (1) - Liquid Excess molar volume, m3/mol - Liquid
298.15 0.0589 -3.5100e-08
298.15 0.1256 -7.1000e-08
298.15 0.2069 -1.0710e-07
298.15 0.2856 -1.3810e-07
298.15 0.3598 -1.6510e-07
298.15 0.4263 -1.8290e-07
298.15 0.4963 -1.9980e-07
298.15 0.5458 -2.0690e-07
298.15 0.6056 -2.0910e-07
298.15 0.6712 -2.0510e-07
298.15 0.7352 -1.9130e-07
298.15 0.8025 -1.6470e-07
298.15 0.8856 -1.1040e-07
298.15 0.9425 -6.3500e-08
303.15 0.0625 -3.1800e-08
303.15 0.1456 -6.7100e-08
303.15 0.2135 -9.3900e-08
303.15 0.2658 -1.1170e-07
303.15 0.3296 -1.3280e-07
303.15 0.3862 -1.4810e-07
303.15 0.4263 -1.5920e-07
303.15 0.4869 -1.7290e-07
303.15 0.5402 -1.8050e-07
303.15 0.6186 -1.8630e-07
303.15 0.6926 -1.8030e-07
303.15 0.7696 -1.6020e-07
303.15 0.8456 -1.2630e-07
303.15 0.9458 -5.3500e-08
313.15 0.0689 -2.8500e-08
313.15 0.1289 -5.0200e-08
313.15 0.1895 -6.8600e-08
313.15 0.2658 -9.1800e-08
313.15 0.3359 -1.1210e-07
313.15 0.3895 -1.2650e-07
313.15 0.4596 -1.4190e-07
313.15 0.5126 -1.5240e-07
313.15 0.5895 -1.6050e-07
313.15 0.6463 -1.6220e-07
313.15 0.7125 -1.5610e-07
313.15 0.7893 -1.3630e-07
313.15 0.8596 -1.0590e-07
313.15 0.9358 -5.6400e-08
323.15 0.0759 -2.4600e-08
323.15 0.1495 -4.2900e-08
323.15 0.1852 -5.3100e-08
323.15 0.2569 -7.0100e-08
323.15 0.3389 -9.0200e-08
323.15 0.3995 -1.0430e-07
323.15 0.4562 -1.1710e-07
323.15 0.4925 -1.2330e-07
323.15 0.5558 -1.3340e-07
323.15 0.6259 -1.3780e-07
323.15 0.7026 -1.3670e-07
323.15 0.7896 -1.2020e-07
323.15 0.8556 -9.5100e-08
323.15 0.9225 -5.8200e-08
333.15 0.0786 -1.8500e-08
333.15 0.1569 -3.2700e-08
333.15 0.2196 -4.4100e-08
333.15 0.2895 -5.8500e-08
333.15 0.3569 -7.2100e-08
333.15 0.4396 -8.8200e-08
333.15 0.4889 -9.8100e-08
333.15 0.5226 -1.0410e-07
333.15 0.5986 -1.1360e-07
333.15 0.6586 -1.1680e-07
333.15 0.7253 -1.1350e-07
333.15 0.8052 -9.9700e-08
333.15 0.8701 -7.6800e-08
333.15 0.9560 -3.1100e-08
343.15 0.0721 -1.0200e-08
343.15 0.1599 -1.9700e-08
343.15 0.2303 -2.9100e-08
343.15 0.3063 -3.9200e-08
343.15 0.3885 -5.5500e-08
343.15 0.4326 -6.3100e-08
343.15 0.4896 -7.3500e-08
343.15 0.5536 -8.3100e-08
343.15 0.6258 -9.1300e-08
343.15 0.6859 -9.4100e-08
343.15 0.7226 -9.2600e-08
343.15 0.8069 -8.3300e-08
343.15 0.8562 -6.9300e-08
343.15 0.9229 -4.3700e-08
353.15 0.0857 -0.0000
353.15 0.1748 -0.0000
353.15 0.2489 -1.2300e-08
353.15 0.3065 -1.8200e-08
353.15 0.3569 -2.5700e-08
353.15 0.4185 -3.5400e-08
353.15 0.4852 -4.7600e-08
353.15 0.5263 -5.4600e-08
353.15 0.5965 -6.5100e-08
353.15 0.6756 -7.3500e-08
353.15 0.7519 -7.3500e-08
353.15 0.8077 -6.7000e-08
353.15 0.8788 -5.2400e-08
353.15 0.9551 -2.3500e-08

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Toluene (1) - Liquid Excess molar volume, m3/mol - Liquid
298.15 0.0589 -3.5100e-08
298.15 0.1256 -7.1000e-08
298.15 0.2069 -1.0710e-07
298.15 0.2856 -1.3810e-07
298.15 0.3598 -1.6510e-07
298.15 0.4263 -1.8290e-07
298.15 0.4963 -1.9980e-07
298.15 0.5458 -2.0690e-07
298.15 0.6056 -2.0910e-07
298.15 0.6712 -2.0510e-07
298.15 0.7352 -1.9130e-07
298.15 0.8025 -1.6470e-07
298.15 0.8856 -1.1040e-07
298.15 0.9425 -6.3500e-08
303.15 0.0625 -3.1800e-08
303.15 0.1456 -6.7100e-08
303.15 0.2135 -9.3900e-08
303.15 0.2658 -1.1170e-07
303.15 0.3296 -1.3280e-07
303.15 0.3862 -1.4810e-07
303.15 0.4263 -1.5920e-07
303.15 0.4869 -1.7290e-07
303.15 0.5402 -1.8050e-07
303.15 0.6186 -1.8630e-07
303.15 0.6926 -1.8030e-07
303.15 0.7696 -1.6020e-07
303.15 0.8456 -1.2630e-07
303.15 0.9458 -5.3500e-08
313.15 0.0689 -2.8500e-08
313.15 0.1289 -5.0200e-08
313.15 0.1895 -6.8600e-08
313.15 0.2658 -9.1800e-08
313.15 0.3359 -1.1210e-07
313.15 0.3895 -1.2650e-07
313.15 0.4596 -1.4190e-07
313.15 0.5126 -1.5240e-07
313.15 0.5895 -1.6050e-07
313.15 0.6463 -1.6220e-07
313.15 0.7125 -1.5610e-07
313.15 0.7893 -1.3630e-07
313.15 0.8596 -1.0590e-07
313.15 0.9358 -5.6400e-08
323.15 0.0759 -2.4600e-08
323.15 0.1495 -4.2900e-08
323.15 0.1852 -5.3100e-08
323.15 0.2569 -7.0100e-08
323.15 0.3389 -9.0200e-08
323.15 0.3995 -1.0430e-07
323.15 0.4562 -1.1710e-07
323.15 0.4925 -1.2330e-07
323.15 0.5558 -1.3340e-07
323.15 0.6259 -1.3780e-07
323.15 0.7026 -1.3670e-07
323.15 0.7896 -1.2020e-07
323.15 0.8556 -9.5100e-08
323.15 0.9225 -5.8200e-08
333.15 0.0786 -1.8500e-08
333.15 0.1569 -3.2700e-08
333.15 0.2196 -4.4100e-08
333.15 0.2895 -5.8500e-08
333.15 0.3569 -7.2100e-08
333.15 0.4396 -8.8200e-08
333.15 0.4889 -9.8100e-08
333.15 0.5226 -1.0410e-07
333.15 0.5986 -1.1360e-07
333.15 0.6586 -1.1680e-07
333.15 0.7253 -1.1350e-07
333.15 0.8052 -9.9700e-08
333.15 0.8701 -7.6800e-08
333.15 0.9560 -3.1100e-08
343.15 0.0721 -1.0200e-08
343.15 0.1599 -1.9700e-08
343.15 0.2303 -2.9100e-08
343.15 0.3063 -3.9200e-08
343.15 0.3885 -5.5500e-08
343.15 0.4326 -6.3100e-08
343.15 0.4896 -7.3500e-08
343.15 0.5536 -8.3100e-08
343.15 0.6258 -9.1300e-08
343.15 0.6859 -9.4100e-08
343.15 0.7226 -9.2600e-08
343.15 0.8069 -8.3300e-08
343.15 0.8562 -6.9300e-08
343.15 0.9229 -4.3700e-08
353.15 0.0857 -0.0000
353.15 0.1748 -0.0000
353.15 0.2489 -1.2300e-08
353.15 0.3065 -1.8200e-08
353.15 0.3569 -2.5700e-08
353.15 0.4185 -3.5400e-08
353.15 0.4852 -4.7600e-08
353.15 0.5263 -5.4600e-08
353.15 0.5965 -6.5100e-08
353.15 0.6756 -7.3500e-08
353.15 0.7519 -7.3500e-08
353.15 0.8077 -6.7000e-08
353.15 0.8788 -5.2400e-08
353.15 0.9551 -2.3500e-08

Sources