Mixture of p-Xylene + Cyclohexanone

Excel

p-Xylene

Name
p-Xylene
InChI
InChI=1S/C8H10/c1-7-3-5-8(2)6-4-7/h3-6H,1-2H3
InChI Key
URLKBWYHVLBVBO-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1ccc(C)cc1
Mol. Weight (g/mol)
106.17
CAS
106-42-3

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
0.0195 0.0196
0.1250 0.0998
0.2706 0.1895
0.3979 0.2760
0.5034 0.3636
0.5245 0.3839
0.5819 0.4391
0.6485 0.5079
0.6824 0.5463
0.7470 0.6251
0.7885 0.6793
0.8025 0.6984
0.8650 0.7850
0.8960 0.8322
0.9311 0.8862

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
0.0195 0.0196
0.1250 0.0998
0.2706 0.1895
0.3979 0.2760
0.5034 0.3636
0.5245 0.3839
0.5819 0.4391
0.6485 0.5079
0.6824 0.5463
0.7470 0.6251
0.7885 0.6793
0.8025 0.6984
0.8650 0.7850
0.8960 0.8322
0.9311 0.8862

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
0.0195 411.55
0.1250 411.85
0.2706 413.25
0.3979 414.85
0.5034 416.65
0.5245 417.05
0.5819 418.25
0.6485 419.65
0.6824 420.45
0.7470 421.95
0.7885 423.05
0.8025 423.35
0.8650 425.05
0.8960 425.75
0.9311 426.75

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
0.0195 411.55
0.1250 411.85
0.2706 413.25
0.3979 414.85
0.5034 416.65
0.5245 417.05
0.5819 418.25
0.6485 419.65
0.6824 420.45
0.7470 421.95
0.7885 423.05
0.8025 423.35
0.8650 425.05
0.8960 425.75
0.9311 426.75

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of p-Xylene (1) - Liquid Excess molar volume, m3/mol - Liquid
293.15 0.0924 1.9500e-08
293.15 0.1647 2.8300e-08
293.15 0.2258 2.5900e-08
293.15 0.2845 2.4100e-08
293.15 0.3589 1.2100e-08
293.15 0.4237 -0.0000
293.15 0.4957 -1.6200e-08
293.15 0.5528 -2.8400e-08
293.15 0.6124 -3.9200e-08
293.15 0.6822 -4.5900e-08
293.15 0.7244 -4.8800e-08
293.15 0.7932 -4.8900e-08
293.15 0.8624 -4.1200e-08
293.15 0.9487 -1.8300e-08
303.15 0.0631 1.5400e-08
303.15 0.1258 2.4400e-08
303.15 0.1842 2.9500e-08
303.15 0.2771 2.4500e-08
303.15 0.3583 1.6800e-08
303.15 0.4257 0.0000
303.15 0.4839 -0.0000
303.15 0.5589 -2.3500e-08
303.15 0.6357 -3.8300e-08
303.15 0.6841 -4.0100e-08
303.15 0.7523 -4.5100e-08
303.15 0.8032 -4.2600e-08
303.15 0.8813 -3.1600e-08
303.15 0.9534 -1.4800e-08
313.15 0.0793 1.8500e-08
313.15 0.1423 2.8400e-08
313.15 0.2189 3.0500e-08
313.15 0.2738 2.9300e-08
313.15 0.3687 1.8300e-08
313.15 0.4234 0.0000
313.15 0.4871 -0.0000
313.15 0.5311 -1.2100e-08
313.15 0.6032 -2.4500e-08
313.15 0.6834 -3.3100e-08
313.15 0.7598 -3.6700e-08
313.15 0.8388 -3.3100e-08
313.15 0.9158 -2.2200e-08
323.15 0.0683 1.6500e-08
323.15 0.1387 2.8400e-08
323.15 0.1944 3.1300e-08
323.15 0.2843 3.0100e-08
323.15 0.3623 2.0800e-08
323.15 0.4134 1.3500e-08
323.15 0.4732 0.0000
323.15 0.5248 -0.0000
323.15 0.6082 -2.0100e-08
323.15 0.6723 -2.8200e-08
323.15 0.7384 -3.1100e-08
323.15 0.8531 -2.7600e-08
323.15 0.9489 -1.1900e-08
333.15 0.0902 2.0500e-08
333.15 0.1423 2.9400e-08
333.15 0.2148 3.2500e-08
333.15 0.2843 3.1300e-08
333.15 0.3765 2.3200e-08
333.15 0.4234 1.7500e-08
333.15 0.4938 0.0000
333.15 0.5421 -0.0000
333.15 0.6133 -1.3400e-08
333.15 0.6455 -1.7300e-08
333.15 0.7249 -2.3100e-08
333.15 0.7832 -2.5600e-08
333.15 0.8634 -2.0900e-08
333.15 0.9457 -1.0500e-08
343.15 0.0743 1.7500e-08
343.15 0.1423 2.8300e-08
343.15 0.2145 3.5000e-08
343.15 0.2843 3.3100e-08
343.15 0.3578 2.8300e-08
343.15 0.4287 2.0500e-08
343.15 0.4927 1.0400e-08
343.15 0.5427 0.0000
343.15 0.6056 -0.0000
343.15 0.6532 -1.1500e-08
343.15 0.7244 -1.7100e-08
343.15 0.7835 -1.7600e-08
343.15 0.8623 -1.6200e-08
343.15 0.9308 -1.0200e-08
353.15 0.0642 1.6500e-08
353.15 0.1393 2.9400e-08
353.15 0.2248 3.7500e-08
353.15 0.2678 3.9500e-08
353.15 0.3408 3.4800e-08
353.15 0.4149 2.7500e-08
353.15 0.4723 2.0400e-08
353.15 0.5234 1.3500e-08
353.15 0.6044 0.0000
353.15 0.6428 -0.0000
353.15 0.7234 -0.0000
353.15 0.8022 -1.2600e-08
353.15 0.8723 -0.0000
353.15 0.9457 -0.0000

Excess molar volume, m3/mol [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of p-Xylene (1) - Liquid Excess molar volume, m3/mol - Liquid
293.15 0.0924 1.9500e-08
293.15 0.1647 2.8300e-08
293.15 0.2258 2.5900e-08
293.15 0.2845 2.4100e-08
293.15 0.3589 1.2100e-08
293.15 0.4237 -0.0000
293.15 0.4957 -1.6200e-08
293.15 0.5528 -2.8400e-08
293.15 0.6124 -3.9200e-08
293.15 0.6822 -4.5900e-08
293.15 0.7244 -4.8800e-08
293.15 0.7932 -4.8900e-08
293.15 0.8624 -4.1200e-08
293.15 0.9487 -1.8300e-08
303.15 0.0631 1.5400e-08
303.15 0.1258 2.4400e-08
303.15 0.1842 2.9500e-08
303.15 0.2771 2.4500e-08
303.15 0.3583 1.6800e-08
303.15 0.4257 0.0000
303.15 0.4839 -0.0000
303.15 0.5589 -2.3500e-08
303.15 0.6357 -3.8300e-08
303.15 0.6841 -4.0100e-08
303.15 0.7523 -4.5100e-08
303.15 0.8032 -4.2600e-08
303.15 0.8813 -3.1600e-08
303.15 0.9534 -1.4800e-08
313.15 0.0793 1.8500e-08
313.15 0.1423 2.8400e-08
313.15 0.2189 3.0500e-08
313.15 0.2738 2.9300e-08
313.15 0.3687 1.8300e-08
313.15 0.4234 0.0000
313.15 0.4871 -0.0000
313.15 0.5311 -1.2100e-08
313.15 0.6032 -2.4500e-08
313.15 0.6834 -3.3100e-08
313.15 0.7598 -3.6700e-08
313.15 0.8388 -3.3100e-08
313.15 0.9158 -2.2200e-08
323.15 0.0683 1.6500e-08
323.15 0.1387 2.8400e-08
323.15 0.1944 3.1300e-08
323.15 0.2843 3.0100e-08
323.15 0.3623 2.0800e-08
323.15 0.4134 1.3500e-08
323.15 0.4732 0.0000
323.15 0.5248 -0.0000
323.15 0.6082 -2.0100e-08
323.15 0.6723 -2.8200e-08
323.15 0.7384 -3.1100e-08
323.15 0.8531 -2.7600e-08
323.15 0.9489 -1.1900e-08
333.15 0.0902 2.0500e-08
333.15 0.1423 2.9400e-08
333.15 0.2148 3.2500e-08
333.15 0.2843 3.1300e-08
333.15 0.3765 2.3200e-08
333.15 0.4234 1.7500e-08
333.15 0.4938 0.0000
333.15 0.5421 -0.0000
333.15 0.6133 -1.3400e-08
333.15 0.6455 -1.7300e-08
333.15 0.7249 -2.3100e-08
333.15 0.7832 -2.5600e-08
333.15 0.8634 -2.0900e-08
333.15 0.9457 -1.0500e-08
343.15 0.0743 1.7500e-08
343.15 0.1423 2.8300e-08
343.15 0.2145 3.5000e-08
343.15 0.2843 3.3100e-08
343.15 0.3578 2.8300e-08
343.15 0.4287 2.0500e-08
343.15 0.4927 1.0400e-08
343.15 0.5427 0.0000
343.15 0.6056 -0.0000
343.15 0.6532 -1.1500e-08
343.15 0.7244 -1.7100e-08
343.15 0.7835 -1.7600e-08
343.15 0.8623 -1.6200e-08
343.15 0.9308 -1.0200e-08
353.15 0.0642 1.6500e-08
353.15 0.1393 2.9400e-08
353.15 0.2248 3.7500e-08
353.15 0.2678 3.9500e-08
353.15 0.3408 3.4800e-08
353.15 0.4149 2.7500e-08
353.15 0.4723 2.0400e-08
353.15 0.5234 1.3500e-08
353.15 0.6044 0.0000
353.15 0.6428 -0.0000
353.15 0.7234 -0.0000
353.15 0.8022 -1.2600e-08
353.15 0.8723 -0.0000
353.15 0.9457 -0.0000

Sources