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 182
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
| 2 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
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Constant Value
Data Table
| x1 [mol/mol] |
y1 [mol/mol] |
| 0.05000 |
0.06800 |
| 0.10000 |
0.13400 |
| 0.20000 |
0.25700 |
| 0.30000 |
0.37600 |
| 0.40000 |
0.48000 |
| 0.50000 |
0.57800 |
| 0.60000 |
0.66300 |
| 0.70000 |
0.75000 |
| 0.80000 |
0.84100 |
| 0.90000 |
0.92500 |
(x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Othmer D.F.: Composition of Vapors from Boiling Binary Solutions. Ind.Eng.Chem. 35 (1943) 614-620 |
Vapor-Liquid Equilibrium Data Set 2013
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
| 2 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 398.35 |
0.03800 |
0.04400 |
| 397.05 |
0.14900 |
0.18200 |
| 397.15 |
0.19800 |
0.22400 |
| 395.25 |
0.28800 |
0.36600 |
| 395.25 |
0.34800 |
0.44100 |
| 394.25 |
0.49100 |
0.58100 |
| 393.75 |
0.55500 |
0.63600 |
| 393.85 |
0.56400 |
0.65700 |
| 393.55 |
0.57600 |
0.67900 |
| 393.15 |
0.61900 |
0.70500 |
| 393.15 |
0.65800 |
0.73800 |
| 392.75 |
0.73400 |
0.78500 |
| 391.65 |
0.83500 |
0.88200 |
| 391.55 |
0.89900 |
0.92700 |
| 391.05 |
0.90900 |
0.92900 |
| 390.85 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Hirata M.; Hirose Y.: Vapor-Liquid Equilibria of Ternary System Water-Acetic Acid-n-Butyl Acetate. Chem.Eng.Japan abridg.Ed. 4 (1966) 238-241 |
Vapor-Liquid Equilibrium Data Set 3914
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
| 2 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
Search the DDB for all data of this mixture
Constant Value
Data Table
| x1 [mol/mol] |
y1 [mol/mol] |
| 0.05000 |
0.06130 |
| 0.11660 |
0.14180 |
| 0.13130 |
0.15960 |
| 0.21450 |
0.25800 |
| 0.38370 |
0.44380 |
| 0.49250 |
0.55290 |
| 0.59550 |
0.65200 |
| 0.71900 |
0.76500 |
| 0.77300 |
0.81280 |
| 0.89500 |
0.91200 |
| 0.90900 |
0.92500 |
| 0.93600 |
0.94500 |
| 0.93800 |
0.94700 |
| 0.96100 |
0.96700 |
| 0.96200 |
0.96700 |
(x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Bushmakin I.N.; Lutugina N.V.: Communication VIII.. J.Appl.Chem.USSR 29 (1956) 1267-1272 |
Diagrams
List of All References
| Source |
| Othmer D.F.: Composition of Vapors from Boiling Binary Solutions. Ind.Eng.Chem. 35 (1943) 614-620 |
| Hirata M.; Hirose Y.: Vapor-Liquid Equilibria of Ternary System Water-Acetic Acid-n-Butyl Acetate. Chem.Eng.Japan abridg.Ed. 4 (1966) 238-241 |
| Bushmakin I.N.; Lutugina N.V.: Communication VIII.. J.Appl.Chem.USSR 29 (1956) 1267-1272 |
Vapor-Liquid Equilibrium Data Overview
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