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 4888
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
2 |
C2H6O2 |
62.068 |
107-21-1 |
1,2-Ethanediol |
Search the DDB for all data of this mixture
Constant Value
Data Table
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
468.85 |
0.00000 |
0.00000 |
462.05 |
0.00380 |
0.19130 |
448.15 |
0.01330 |
0.47160 |
427.55 |
0.04000 |
0.74450 |
422.35 |
0.05150 |
0.79000 |
407.15 |
0.12470 |
0.88300 |
405.35 |
0.18490 |
0.88600 |
404.45 |
0.31710 |
0.88900 |
404.45 |
0.42870 |
0.88900 |
404.45 |
0.51590 |
0.88900 |
404.45 |
0.52740 |
0.88900 |
403.95 |
0.66620 |
0.90200 |
403.65 |
0.68980 |
0.90600 |
403.25 |
0.73450 |
0.91450 |
401.65 |
0.83050 |
0.93500 |
400.55 |
0.87400 |
0.94600 |
399.75 |
0.92080 |
0.96200 |
399.15 |
0.94840 |
0.97400 |
397.85 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Mainkar S.V.; Mene P.S.: Binary Vapour Liquid Equilibria for n-Butanol Ethylene Glycol & n-Butyl Acetate-Ethylene Glycol Systems. Indian J.Technol. 8 (1970) 320-322 |
Diagrams
List of All References
Source |
Mainkar S.V.; Mene P.S.: Binary Vapour Liquid Equilibria for n-Butanol Ethylene Glycol & n-Butyl Acetate-Ethylene Glycol Systems. Indian J.Technol. 8 (1970) 320-322 |
Vapor-Liquid Equilibrium Data Overview
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