Mixture of 1,2-Ethanediol, diacetate + 1,2-Ethanediol, monoacetate

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1,2-Ethanediol, diacetate

Name
1,2-Ethanediol, diacetate
InChI
InChI=1S/C6H10O4/c1-5(7)9-3-4-10-6(2)8/h3-4H2,1-2H3
InChI Key
JTXMVXSTHSMVQF-UHFFFAOYSA-N
Formula
C6H10O4
SMILES
CC(=O)OCCOC(C)=O
Mol. Weight (g/mol)
146.14
CAS
111-55-7

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

Datasets

  1. Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
  2. Vapor or sublimation pressure, kPa
  3. Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
  4. Vapor or sublimation pressure, kPa
  5. Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
  6. Vapor or sublimation pressure, kPa
  7. Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
  8. Vapor or sublimation pressure, kPa

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

Operational conditions:

Mole fraction of 1,2-Ethanediol, monoacetate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1030 0.2880
0.2310 0.5450
0.3777 0.6830
0.5367 0.6990
0.7024 0.5960
0.8299 0.4100
0.9272 0.2070

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 363.15 (Liquid)

Mole fraction of 1,2-Ethanediol, diacetate (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 2.23
0.0019 2.24
0.0040 2.24
0.0059 2.26
0.0107 2.27
0.0199 2.29
0.0421 2.35
0.0703 2.40
0.1068 2.45
0.1541 2.51
0.2134 2.58
0.2789 2.63
0.3461 2.67
0.4174 2.70
0.4852 2.73
0.5624 2.76
0.6458 2.78
0.7293 2.79
0.8023 2.80
0.8631 2.79
0.9131 2.79
0.9545 2.79
0.9748 2.78
0.9852 2.77
0.9901 2.77
0.9950 2.76
1.0000 2.74

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

Operational conditions:

Mole fraction of 1,2-Ethanediol, monoacetate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1030 0.2880
0.2310 0.5450
0.3777 0.6830
0.5367 0.6990
0.7024 0.5960
0.8299 0.4100
0.9272 0.2070

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 363.15 (Liquid)

Mole fraction of 1,2-Ethanediol, diacetate (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 2.23
0.0019 2.24
0.0040 2.24
0.0059 2.26
0.0107 2.27
0.0199 2.29
0.0421 2.35
0.0703 2.40
0.1068 2.45
0.1541 2.51
0.2134 2.58
0.2789 2.63
0.3461 2.67
0.4174 2.70
0.4852 2.73
0.5624 2.76
0.6458 2.78
0.7293 2.79
0.8023 2.80
0.8631 2.79
0.9131 2.79
0.9545 2.79
0.9748 2.78
0.9852 2.77
0.9901 2.77
0.9950 2.76
1.0000 2.74

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

Operational conditions:

Mole fraction of 1,2-Ethanediol, monoacetate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1030 0.2880
0.2310 0.5450
0.3777 0.6830
0.5367 0.6990
0.7024 0.5960
0.8299 0.4100
0.9272 0.2070

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 363.15 (Liquid)

Mole fraction of 1,2-Ethanediol, diacetate (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 2.23
0.0019 2.24
0.0040 2.24
0.0059 2.26
0.0107 2.27
0.0199 2.29
0.0421 2.35
0.0703 2.40
0.1068 2.45
0.1541 2.51
0.2134 2.58
0.2789 2.63
0.3461 2.67
0.4174 2.70
0.4852 2.73
0.5624 2.76
0.6458 2.78
0.7293 2.79
0.8023 2.80
0.8631 2.79
0.9131 2.79
0.9545 2.79
0.9748 2.78
0.9852 2.77
0.9901 2.77
0.9950 2.76
1.0000 2.74

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

Operational conditions:

Mole fraction of 1,2-Ethanediol, monoacetate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1030 0.2880
0.2310 0.5450
0.3777 0.6830
0.5367 0.6990
0.7024 0.5960
0.8299 0.4100
0.9272 0.2070

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 363.15 (Liquid)

Mole fraction of 1,2-Ethanediol, diacetate (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
0.0000 2.23
0.0019 2.24
0.0040 2.24
0.0059 2.26
0.0107 2.27
0.0199 2.29
0.0421 2.35
0.0703 2.40
0.1068 2.45
0.1541 2.51
0.2134 2.58
0.2789 2.63
0.3461 2.67
0.4174 2.70
0.4852 2.73
0.5624 2.76
0.6458 2.78
0.7293 2.79
0.8023 2.80
0.8631 2.79
0.9131 2.79
0.9545 2.79
0.9748 2.78
0.9852 2.77
0.9901 2.77
0.9950 2.76
1.0000 2.74

Sources

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