Mixture of 1,2-Ethanediol + Neopentyl glycol

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1,2-Ethanediol

Name
1,2-Ethanediol
InChI
InChI=1S/C2H6O2/c3-1-2-4/h3-4H,1-2H2
InChI Key
LYCAIKOWRPUZTN-UHFFFAOYSA-N
Formula
C2H6O2
SMILES
OCCO
Mol. Weight (g/mol)
62.07
CAS
107-21-1

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 1,2-Ethanediol (1) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,2-Ethanediol (1) - Liquid Mole fraction of 1,2-Ethanediol (1) - Gas
470.22 1.0000 1.0000
470.80 0.9242 0.9382
471.28 0.8524 0.8763
471.77 0.7727 0.8047
472.29 0.6841 0.7216
472.71 0.6115 0.6518
473.31 0.4966 0.5394
473.76 0.4165 0.4601
474.79 0.2439 0.2870
475.76 0.1333 0.1696
476.63 0.0587 0.0813
478.95 0.0000 0.0000

Mole fraction of 1,2-Ethanediol (1) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,2-Ethanediol (1) - Liquid Mole fraction of 1,2-Ethanediol (1) - Gas
470.22 1.0000 1.0000
470.80 0.9242 0.9382
471.28 0.8524 0.8763
471.77 0.7727 0.8047
472.29 0.6841 0.7216
472.71 0.6115 0.6518
473.31 0.4966 0.5394
473.76 0.4165 0.4601
474.79 0.2439 0.2870
475.76 0.1333 0.1696
476.63 0.0587 0.0813
478.95 0.0000 0.0000

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1,2-Ethanediol (1) - Liquid Boiling temperature at pressure P, K - Liquid
1.0000 470.22
0.9242 470.80
0.8524 471.28
0.7727 471.77
0.6841 472.29
0.6115 472.71
0.4966 473.31
0.4165 473.76
0.2439 474.79
0.1333 475.76
0.0587 476.63
0.0000 478.95

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of 1,2-Ethanediol (1) - Liquid Boiling temperature at pressure P, K - Liquid
1.0000 470.22
0.9242 470.80
0.8524 471.28
0.7727 471.77
0.6841 472.29
0.6115 472.71
0.4966 473.31
0.4165 473.76
0.2439 474.79
0.1333 475.76
0.0587 476.63
0.0000 478.95

Sources