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 579
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 |
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Constant Value
Data Table
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
351.45 |
0.00000 |
0.00000 |
349.55 |
0.03300 |
0.11100 |
347.15 |
0.07800 |
0.21600 |
343.95 |
0.14900 |
0.34500 |
342.25 |
0.19500 |
0.41000 |
338.75 |
0.31600 |
0.53400 |
336.55 |
0.41400 |
0.61400 |
334.45 |
0.53200 |
0.69700 |
332.15 |
0.69100 |
0.79600 |
330.45 |
0.85200 |
0.89600 |
329.25 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Amer H.H.; Paxton R.R.; van Winkle M.: Vapor-liquid equilibria. Ind.Eng.Chem. 48 (1956) 142-146 |
Vapor-Liquid Equilibrium Data Set 581
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 |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
11.679 |
0.00000 |
14.999 |
0.04220 |
16.585 |
0.06730 |
19.358 |
0.11300 |
22.571 |
0.17870 |
24.811 |
0.23610 |
25.585 |
0.26650 |
27.384 |
0.31280 |
28.371 |
0.34700 |
31.037 |
0.44580 |
33.037 |
0.53720 |
35.370 |
0.65480 |
37.584 |
0.77210 |
38.890 |
0.84740 |
40.130 |
0.92520 |
41.317 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
Source |
Gordon A.R.; Hines W.G.: Liquid-vapour equilibrium for the system ethanol-acetone. Can.J.Res.Sec.B 24 (1946) 254-262 |
Vapor-Liquid Equilibrium Data Set 582
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 |
Search the DDB for all data of this mixture
Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
17.892 |
0.00000 |
21.612 |
0.03890 |
22.012 |
0.04460 |
24.531 |
0.07650 |
29.211 |
0.14090 |
32.011 |
0.18830 |
36.037 |
0.26830 |
39.037 |
0.34060 |
42.463 |
0.43550 |
45.410 |
0.53150 |
48.796 |
0.65280 |
51.729 |
0.77270 |
53.716 |
0.85930 |
54.689 |
0.90380 |
56.649 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
Source |
Gordon A.R.; Hines W.G.: Liquid-vapour equilibrium for the system ethanol-acetone. Can.J.Res.Sec.B 24 (1946) 254-262 |
Diagrams
List of All References
Source |
Amer H.H.; Paxton R.R.; van Winkle M.: Vapor-liquid equilibria. Ind.Eng.Chem. 48 (1956) 142-146 |
Gordon A.R.; Hines W.G.: Liquid-vapour equilibrium for the system ethanol-acetone. Can.J.Res.Sec.B 24 (1946) 254-262 |
Vapor-Liquid Equilibrium Data Overview
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