Mixture of 1,2-Ethanediol, monoacetate + Water

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1,2-Ethanediol, monoacetate

Name
1,2-Ethanediol, monoacetate
InChI
InChI=1S/C4H8O3/c1-4(6)7-3-2-5/h5H,2-3H2,1H3
InChI Key
HXDLWJWIAHWIKI-UHFFFAOYSA-N
Formula
C4H8O3
SMILES
CC(=O)OCCO
Mol. Weight (g/mol)
104.10
CAS
542-59-6

Water

Name
Water
InChI
InChI=1S/H2O/h1H2
InChI Key
XLYOFNOQVPJJNP-UHFFFAOYSA-N
Formula
H2O
SMILES
O
Mol. Weight (g/mol)
18.02
CAS
7732-18-5
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. Pvap - Vapor or sublimation pressure, kPa (2)

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Water (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1179 -0.8030
0.2578 -0.7380
0.3978 -0.4890
0.5460 -0.3040
0.6907 -0.1560
0.8250 -0.0706
0.9399 -0.0200

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Water (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1179 -0.8030
0.2578 -0.7380
0.3978 -0.4890
0.5460 -0.3040
0.6907 -0.1560
0.8250 -0.0706
0.9399 -0.0200

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 363.15 (Liquid)

Mole fraction of Water (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 2.25
0.0235 4.68
0.0589 8.24
0.0795 10.25
0.1277 14.85
0.3086 30.21
0.4058 38.29
0.5049 45.54
0.5986 51.63
0.6831 56.34
0.7509 59.64
0.8033 61.87
0.8054 62.11
0.8409 63.53
0.8419 63.43
0.8712 64.57
0.8743 64.83
0.9051 65.97
0.9314 67.01
0.9527 67.89
0.9683 68.58
0.9795 69.11
0.9878 69.48
0.9941 69.87
0.9969 69.98
0.9982 70.00
0.9988 70.00
0.9994 69.95
1.0000 69.93

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 363.15 (Liquid)

Mole fraction of Water (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 2.25
0.0235 4.68
0.0589 8.24
0.0795 10.25
0.1277 14.85
0.3086 30.21
0.4058 38.29
0.5049 45.54
0.5986 51.63
0.6831 56.34
0.7509 59.64
0.8033 61.87
0.8054 62.11
0.8409 63.53
0.8419 63.43
0.8712 64.57
0.8743 64.83
0.9051 65.97
0.9314 67.01
0.9527 67.89
0.9683 68.58
0.9795 69.11
0.9878 69.48
0.9941 69.87
0.9969 69.98
0.9982 70.00
0.9988 70.00
0.9994 69.95
1.0000 69.93

Sources