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 22417
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 365.65 |
0.10030 |
0.19990 |
0.36920 |
0.36650 |
| 362.35 |
0.10020 |
0.29820 |
0.35750 |
0.45050 |
| 355.65 |
0.09980 |
0.49990 |
0.34300 |
0.54420 |
| 348.65 |
0.10070 |
0.79840 |
0.23240 |
0.74620 |
| 360.55 |
0.20030 |
0.10020 |
0.62760 |
0.16550 |
| 354.25 |
0.20040 |
0.29960 |
0.48680 |
0.40680 |
| 348.15 |
0.19980 |
0.49090 |
0.46190 |
0.48370 |
| 343.95 |
0.20020 |
0.69710 |
0.43190 |
0.55370 |
| 347.65 |
0.40090 |
0.10000 |
0.81240 |
0.08510 |
| 343.55 |
0.39990 |
0.29990 |
0.73620 |
0.20740 |
| 339.55 |
0.40050 |
0.49900 |
0.65320 |
0.32940 |
| 339.15 |
0.60010 |
0.09990 |
0.87220 |
0.07370 |
| 337.35 |
0.59980 |
0.19990 |
0.81960 |
0.14480 |
| 335.75 |
0.60000 |
0.29980 |
0.79890 |
0.18600 |
| 336.25 |
0.70030 |
0.09940 |
0.89090 |
0.07490 |
| 334.75 |
0.69980 |
0.20010 |
0.87000 |
0.11560 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Pustilnik T.M.; Remizer G.P.; Taravikov G.M.; Perelygin V.M.: . Oniitekhim (1980) 1-11 |
Vapor-Liquid Equilibrium Data Set 30444
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
| 329.85 |
0.90000 |
0.05000 |
| 331.25 |
0.80000 |
0.10000 |
| 333.65 |
0.70000 |
0.10000 |
| 334.15 |
0.60000 |
0.30000 |
| 337.85 |
0.50000 |
0.20000 |
| 338.15 |
0.40000 |
0.40000 |
| 339.85 |
0.40000 |
0.30000 |
| 340.45 |
0.30000 |
0.50000 |
| 341.25 |
0.40000 |
0.20000 |
| 341.65 |
0.30000 |
0.40000 |
| 341.65 |
0.20000 |
0.70000 |
| 343.25 |
0.30000 |
0.30000 |
| 345.15 |
0.10000 |
0.80000 |
| 346.05 |
0.20000 |
0.40000 |
| 347.25 |
0.30000 |
0.10000 |
| 347.35 |
0.05000 |
0.90000 |
| 348.35 |
0.20000 |
0.30000 |
| 348.55 |
0.10000 |
0.60000 |
| 354.35 |
0.20000 |
0.10000 |
| 360.15 |
0.10000 |
0.20000 |
| 364.35 |
0.10000 |
0.10000 |
(T - temperature, x - liquid mole fraction)
Reference
| Source |
| Mehta S.C.; Mene P.S.: On Ternary Vapour - Liquid Equilibrium Data Acetone - Ethanol - n-Butanol System. Indian Chem.Eng. 8 (1966) 17-20 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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