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 158
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 290.75 |
0.06340 |
0.13810 |
| 288.95 |
0.11460 |
0.23680 |
| 285.75 |
0.22130 |
0.36470 |
| 283.95 |
0.34640 |
0.50610 |
| 282.35 |
0.56870 |
0.69490 |
| 281.15 |
0.76490 |
0.80940 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Fordyce C.R.; Simonsen D.R.: Evaporation in Binary Solvent Mixtures. Ind.Eng.Chem. 41 (1949) 104-111 |
Vapor-Liquid Equilibrium Data Set 586
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 337.75 |
0.00000 |
0.00000 |
| 336.65 |
0.03600 |
0.08200 |
| 335.35 |
0.08100 |
0.16100 |
| 333.85 |
0.14100 |
0.25100 |
| 332.55 |
0.20600 |
0.33600 |
| 331.25 |
0.29300 |
0.42300 |
| 330.05 |
0.39400 |
0.50000 |
| 329.35 |
0.51300 |
0.58000 |
| 329.05 |
0.58400 |
0.63900 |
| 328.95 |
0.68300 |
0.70500 |
| 328.95 |
0.74200 |
0.74500 |
| 328.95 |
0.82300 |
0.80600 |
| 328.95 |
0.86100 |
0.84300 |
| 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 587
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 335.95 |
0.06000 |
0.09700 |
| 333.95 |
0.15000 |
0.25000 |
| 331.75 |
0.29500 |
0.42000 |
| 330.35 |
0.39800 |
0.51700 |
| 329.45 |
0.52500 |
0.62500 |
| 328.95 |
0.73200 |
0.75400 |
| 328.85 |
0.80000 |
0.80000 |
| 329.05 |
0.89200 |
0.87500 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Griswold J.; Buford C.B.: Separation of synthesis mixtures Vapor-liquid equilibria of acetone-methanol-water. Ind.Eng.Chem. 41 (1949) 2347-2351 |
Diagrams
List of All References
| Source |
| Griswold J.; Buford C.B.: Separation of synthesis mixtures Vapor-liquid equilibria of acetone-methanol-water. Ind.Eng.Chem. 41 (1949) 2347-2351 |
| Amer H.H.; Paxton R.R.; van Winkle M.: Vapor-liquid equilibria. Ind.Eng.Chem. 48 (1956) 142-146 |
| Fordyce C.R.; Simonsen D.R.: Evaporation in Binary Solvent Mixtures. Ind.Eng.Chem. 41 (1949) 104-111 |
Vapor-Liquid Equilibrium Data Overview
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