Dortmund Data Bank
Vapor-Liquid Equilibrium Data
The experimental data shown in these pages are freely available and have been published already in the DDB Explorer Edition. The data represent a small sub list of all available data in the Dortmund Data Bank. For more data or any further information please search the DDB or contact DDBST.
Vapor-Liquid Equilibrium Data Set 135
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
2 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
17.025 |
0.10980 |
0.30550 |
23.585 |
0.24250 |
0.55160 |
29.998 |
0.37250 |
0.71580 |
31.064 |
0.39300 |
0.73320 |
31.197 |
0.39860 |
0.73790 |
35.330 |
0.49390 |
0.81600 |
44.596 |
0.73110 |
0.93900 |
53.382 |
0.90330 |
0.97850 |
53.489 |
0.94100 |
0.98920 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Shmidt L.L.: Zur Untersuchung der Lösungskinetik. Zh.Russ.Fiz.Khim.Obshch.Khim. 62 (1930) 1847-1858 |
Vapor-Liquid Equilibrium Data Set 232
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
2 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
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Constant Value
Data Table
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
381.25 |
0.13800 |
0.32700 |
378.25 |
0.18200 |
0.42200 |
372.85 |
0.28600 |
0.58900 |
366.75 |
0.42000 |
0.73200 |
361.45 |
0.56100 |
0.85400 |
352.65 |
0.87200 |
0.97800 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Garner F.H.; Ellis S.R.M.; Pearce C.J.: Extraction of Acetic from Water. Chem.Eng.Sci. 3 (1954) 48-54 |
Vapor-Liquid Equilibrium Data Set 826
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
2 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
5.133 |
0.00000 |
0.00000 |
9.133 |
0.16320 |
0.47250 |
12.772 |
0.31680 |
0.68920 |
18.932 |
0.57960 |
0.89340 |
21.865 |
0.73120 |
0.94880 |
25.078 |
0.90330 |
0.97870 |
25.878 |
0.92950 |
0.98660 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Shmidt L.L.: Zur Untersuchung der Lösungskinetik. Zh.Russ.Fiz.Khim.Obshch.Khim. 62 (1930) 1847-1858 |
Diagrams
List of All References
Source |
Garner F.H.; Ellis S.R.M.; Pearce C.J.: Extraction of Acetic from Water. Chem.Eng.Sci. 3 (1954) 48-54 |
Shmidt L.L.: Zur Untersuchung der Lösungskinetik. Zh.Russ.Fiz.Khim.Obshch.Khim. 62 (1930) 1847-1858 |
Vapor-Liquid Equilibrium Data Overview
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