Mixture of Diethyl carbonate + Carbonic acid, ethyl-, methyl ester

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Diethyl carbonate

Name
Diethyl carbonate
InChI
InChI=1S/C5H10O3/c1-3-7-5(6)8-4-2/h3-4H2,1-2H3
InChI Key
OIFBSDVPJOWBCH-UHFFFAOYSA-N
Formula
C5H10O3
SMILES
CCOC(=O)OCC
Mol. Weight (g/mol)
118.13
CAS
105-58-8

Carbonic acid, ethyl-, methyl ester

Name
Carbonic acid, ethyl-, methyl ester
InChI
InChI=1S/C4H8O3/c1-3-7-4(5)6-2/h3H2,1-2H3
InChI Key
JBTWLSYIZRCDFO-UHFFFAOYSA-N
Formula
C4H8O3
SMILES
CCOC(=O)OC
Mol. Weight (g/mol)
104.10
CAS
623-53-0
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Datasets

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

Mole fraction of Carbonic acid, ethyl-, methyl ester (2) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Carbonic acid, ethyl-, methyl ester (2) - Liquid Mole fraction of Carbonic acid, ethyl-, methyl ester (2) - Gas
0.0713 0.1126
0.1155 0.1778
0.1978 0.2904
0.2573 0.3678
0.3270 0.4497
0.4135 0.5450
0.5224 0.6550
0.5887 0.7162
0.6514 0.7687
0.7192 0.8218
0.8002 0.8804
0.8660 0.9238

Mole fraction of Carbonic acid, ethyl-, methyl ester (2) [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Carbonic acid, ethyl-, methyl ester (2) - Liquid Mole fraction of Carbonic acid, ethyl-, methyl ester (2) - Gas
0.0713 0.1126
0.1155 0.1778
0.1978 0.2904
0.2573 0.3678
0.3270 0.4497
0.4135 0.5450
0.5224 0.6550
0.5887 0.7162
0.6514 0.7687
0.7192 0.8218
0.8002 0.8804
0.8660 0.9238

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Carbonic acid, ethyl-, methyl ester (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0713 397.95
0.1155 396.95
0.1978 395.15
0.2573 394.15
0.3270 392.65
0.4135 391.15
0.5224 389.25
0.5887 388.15
0.6514 386.95
0.7192 385.65
0.8002 384.50
0.8660 383.25

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.33 (Liquid)

Mole fraction of Carbonic acid, ethyl-, methyl ester (2) - Liquid Boiling temperature at pressure P, K - Liquid
0.0713 397.95
0.1155 396.95
0.1978 395.15
0.2573 394.15
0.3270 392.65
0.4135 391.15
0.5224 389.25
0.5887 388.15
0.6514 386.95
0.7192 385.65
0.8002 384.50
0.8660 383.25

Sources