Mixture of p-Xylene + Neopentyl glycol

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

Neopentyl glycol

Name
Neopentyl glycol
InChI
InChI=1S/C5H12O2/c1-5(2,3-6)4-7/h6-7H,3-4H2,1-2H3
InChI Key
SLCVBVWXLSEKPL-UHFFFAOYSA-N
Formula
C5H12O2
SMILES
CC(C)(CO)CO
Mol. Weight (g/mol)
104.15
CAS
126-30-7
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Datasets

  1. Mole fraction (2)
  2. Tboil - Boiling temperature at pressure P, K (2)

Mole fraction of Neopentyl glycol (2) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Neopentyl glycol (2) - Liquid Mole fraction of Neopentyl glycol (2) - Gas
411.21 0.0000 0.0000
414.70 0.0751 0.0097
419.62 0.2237 0.0218
427.69 0.3512 0.0497
432.33 0.4310 0.0776
442.49 0.5764 0.1631
449.35 0.6626 0.2465
456.64 0.7508 0.3634
466.21 0.8711 0.5824
472.57 0.9468 0.7754
475.19 0.9752 0.8775
478.95 1.0000 1.0000

Mole fraction of Neopentyl glycol (2) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Neopentyl glycol (2) - Liquid Mole fraction of Neopentyl glycol (2) - Gas
411.21 0.0000 0.0000
414.70 0.0751 0.0097
419.62 0.2237 0.0218
427.69 0.3512 0.0497
432.33 0.4310 0.0776
442.49 0.5764 0.1631
449.35 0.6626 0.2465
456.64 0.7508 0.3634
466.21 0.8711 0.5824
472.57 0.9468 0.7754
475.19 0.9752 0.8775
478.95 1.0000 1.0000

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Neopentyl glycol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 411.21
0.0751 414.70
0.2237 419.62
0.3512 427.69
0.4310 432.33
0.5764 442.49
0.6626 449.35
0.7508 456.64
0.8711 466.21
0.9468 472.57
0.9752 475.19
1.0000 478.95

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Neopentyl glycol (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 411.21
0.0751 414.70
0.2237 419.62
0.3512 427.69
0.4310 432.33
0.5764 442.49
0.6626 449.35
0.7508 456.64
0.8711 466.21
0.9468 472.57
0.9752 475.19
1.0000 478.95

Sources