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 256
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 32.797 |
0.12900 |
0.34400 |
| 36.037 |
0.23200 |
0.44000 |
| 37.664 |
0.31100 |
0.50200 |
| 38.663 |
0.39200 |
0.55400 |
| 39.863 |
0.50700 |
0.63200 |
| 39.997 |
0.55200 |
0.64000 |
| 39.863 |
0.64100 |
0.65900 |
| 39.997 |
0.67300 |
0.67500 |
| 39.997 |
0.72100 |
0.70900 |
| 40.130 |
0.76600 |
0.72900 |
| 39.090 |
0.86000 |
0.80800 |
| 38.330 |
0.91100 |
0.85100 |
| 37.197 |
0.95100 |
0.90600 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Bredig G.; Bayer R.: II. Dampfdrucke des ternären Systems Methylalkohol-Methylacetat-Äthylacetat. Z.Phys.Chem.(Leipzig) 130 (1927) 15-28 |
Vapor-Liquid Equilibrium Data Set 445
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 347.95 |
0.01900 |
0.07900 |
| 347.15 |
0.02400 |
0.09300 |
| 345.45 |
0.05600 |
0.18100 |
| 340.25 |
0.18100 |
0.38400 |
| 337.85 |
0.31100 |
0.49200 |
| 337.35 |
0.35000 |
0.52000 |
| 336.75 |
0.40300 |
0.55700 |
| 335.75 |
0.56600 |
0.64000 |
| 335.55 |
0.61600 |
0.67500 |
| 335.55 |
0.64600 |
0.67800 |
| 335.45 |
0.70800 |
0.71100 |
| 335.25 |
0.72000 |
0.71600 |
| 335.45 |
0.73400 |
0.71700 |
| 335.65 |
0.74300 |
0.73200 |
| 335.75 |
0.74400 |
0.73300 |
| 335.65 |
0.81000 |
0.77900 |
| 335.55 |
0.81500 |
0.78400 |
| 335.95 |
0.88900 |
0.84600 |
| 336.45 |
0.93900 |
0.90300 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Akita K.; Yoshida F.: Phase-Equilibria in Methanol-Ethyl Acetate-Water System. J.Chem.Eng.Data 8 (1963) 484-490 |
Vapor-Liquid Equilibrium Data Set 446
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 30.864 |
0.05000 |
0.21150 |
| 30.864 |
0.06700 |
0.21300 |
| 31.997 |
0.09700 |
0.26200 |
| 34.530 |
0.15400 |
0.37180 |
| 35.797 |
0.21750 |
0.42420 |
| 37.864 |
0.26200 |
0.46950 |
| 38.597 |
0.30000 |
0.49120 |
| 39.530 |
0.38200 |
0.53560 |
| 39.730 |
0.45000 |
0.53600 |
| 40.530 |
0.56800 |
0.61500 |
| 40.663 |
0.65600 |
0.66000 |
| 40.263 |
0.71900 |
0.69400 |
| 40.463 |
0.78000 |
0.73000 |
| 40.197 |
0.81000 |
0.74950 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Murti P.S.; van Winkle M.: Vapor-Liquid Equilibria for Binary Systems of Methanol, Ethyl Alcohol, 1-Propanol, and 2-Propanol with Ethyl Acetate and 1-Propanol-Water. Ind.Eng.Chem. Chem.Eng.Data Series 3 (1958) 72-81 |
Diagrams
List of All References
| Source |
| Murti P.S.; van Winkle M.: Vapor-Liquid Equilibria for Binary Systems of Methanol, Ethyl Alcohol, 1-Propanol, and 2-Propanol with Ethyl Acetate and 1-Propanol-Water. Ind.Eng.Chem. Chem.Eng.Data Series 3 (1958) 72-81 |
| Akita K.; Yoshida F.: Phase-Equilibria in Methanol-Ethyl Acetate-Water System. J.Chem.Eng.Data 8 (1963) 484-490 |
| Bredig G.; Bayer R.: II. Dampfdrucke des ternären Systems Methylalkohol-Methylacetat-Äthylacetat. Z.Phys.Chem.(Leipzig) 130 (1927) 15-28 |
Vapor-Liquid Equilibrium Data Overview
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