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 451
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 351.45 |
0.00000 |
0.00000 |
| 349.75 |
0.13400 |
0.18300 |
| 348.15 |
0.24200 |
0.32600 |
| 346.75 |
0.32000 |
0.42800 |
| 345.45 |
0.40100 |
0.52900 |
| 344.85 |
0.43500 |
0.56600 |
| 343.15 |
0.54200 |
0.67600 |
| 341.75 |
0.65200 |
0.75900 |
| 340.85 |
0.72800 |
0.81300 |
| 340.05 |
0.79000 |
0.85800 |
| 339.75 |
0.81400 |
0.87500 |
| 338.95 |
0.87300 |
0.91900 |
| 338.75 |
0.91000 |
0.93700 |
| 337.75 |
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 2120
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 350.15 |
0.07300 |
0.12000 |
| 348.95 |
0.14200 |
0.22200 |
| 347.15 |
0.24800 |
0.36200 |
| 345.45 |
0.37500 |
0.50500 |
| 344.05 |
0.47000 |
0.60000 |
| 342.35 |
0.60000 |
0.72500 |
| 340.75 |
0.72500 |
0.82000 |
| 338.95 |
0.88800 |
0.93200 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Delzenne A.O.: Vapor-Liquid Equilibrium Data for Ternary System Methanol-Ethanol-Water. Ind.Eng.Chem. Chem.Eng.Data Series 3 (1958) 224-230 |
Vapor-Liquid Equilibrium Data Set 2719
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 351.55 |
0.00000 |
0.00000 |
| 351.35 |
0.01200 |
0.02600 |
| 350.45 |
0.05600 |
0.08900 |
| 349.85 |
0.11600 |
0.16200 |
| 349.05 |
0.14200 |
0.19400 |
| 348.65 |
0.16200 |
0.22800 |
| 348.35 |
0.19000 |
0.26100 |
| 347.85 |
0.21400 |
0.29300 |
| 347.45 |
0.24000 |
0.32700 |
| 347.05 |
0.26000 |
0.35700 |
| 346.65 |
0.28700 |
0.38600 |
| 346.15 |
0.31100 |
0.44500 |
| 345.65 |
0.34500 |
0.47000 |
| 345.45 |
0.38000 |
0.49200 |
| 344.15 |
0.43400 |
0.56000 |
| 343.75 |
0.48000 |
0.60000 |
| 343.15 |
0.49700 |
0.63700 |
| 342.45 |
0.56700 |
0.68500 |
| 342.15 |
0.59700 |
0.71600 |
| 341.75 |
0.61000 |
0.73500 |
| 341.45 |
0.63000 |
0.75100 |
| 341.25 |
0.64500 |
0.76300 |
| 340.75 |
0.68300 |
0.79100 |
| 340.65 |
0.71500 |
0.80500 |
| 340.45 |
0.74500 |
0.81800 |
| 340.25 |
0.73100 |
0.82600 |
| 339.55 |
0.78900 |
0.87000 |
| 338.75 |
0.91000 |
0.95000 |
| 337.85 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Slobodyanik I.P.; Babushkina E.M.: Liquid-Liquid Equilibrium in the System Methanol-Ethanol. J.Appl.Chem.USSR 39 (1966) 1782-1783 |
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 |
| Slobodyanik I.P.; Babushkina E.M.: Liquid-Liquid Equilibrium in the System Methanol-Ethanol. J.Appl.Chem.USSR 39 (1966) 1782-1783 |
| Delzenne A.O.: Vapor-Liquid Equilibrium Data for Ternary System Methanol-Ethanol-Water. Ind.Eng.Chem. Chem.Eng.Data Series 3 (1958) 224-230 |
Vapor-Liquid Equilibrium Data Overview
© DDBST GmbH
