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 459
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 2 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 354.15 |
0.10000 |
0.16580 |
| 351.95 |
0.20000 |
0.28890 |
| 350.55 |
0.30000 |
0.38760 |
| 349.55 |
0.40000 |
0.48060 |
| 349.35 |
0.50000 |
0.54980 |
| 349.15 |
0.60000 |
0.62680 |
| 349.55 |
0.70000 |
0.70660 |
| 348.65 |
0.80000 |
0.78360 |
| 349.75 |
0.90000 |
0.88540 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Nishi Y.: Vapor-Liquid Equilibria Accompanied by Hypothetical Chemical Reaction. J.Chem.Eng.Japan 5 (1972) 334-339 |
Vapor-Liquid Equilibrium Data Set 609
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 2 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 15.732 |
0.03800 |
0.13470 |
| 16.065 |
0.05000 |
0.16600 |
| 16.799 |
0.07000 |
0.21750 |
| 18.265 |
0.11550 |
0.30650 |
| 19.798 |
0.15000 |
0.37300 |
| 20.332 |
0.19900 |
0.42300 |
| 21.532 |
0.27000 |
0.49500 |
| 21.865 |
0.29000 |
0.50400 |
| 23.198 |
0.38500 |
0.57800 |
| 23.731 |
0.46150 |
0.62250 |
| 24.465 |
0.54000 |
0.66650 |
| 25.465 |
0.64050 |
0.71200 |
| 25.865 |
0.81400 |
0.81500 |
| 25.598 |
0.90850 |
0.89860 |
(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 |
Vapor-Liquid Equilibrium Data Set 610
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 2 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 41.663 |
0.04550 |
0.12540 |
| 42.863 |
0.07400 |
0.15850 |
| 43.930 |
0.08550 |
0.19000 |
| 44.063 |
0.09350 |
0.21760 |
| 45.730 |
0.12950 |
0.26280 |
| 47.329 |
0.15900 |
0.29800 |
| 47.796 |
0.17550 |
0.32050 |
| 51.329 |
0.26650 |
0.42130 |
| 52.529 |
0.31350 |
0.46130 |
| 53.929 |
0.36000 |
0.48810 |
| 54.862 |
0.42750 |
0.53690 |
| 55.062 |
0.43200 |
0.54130 |
| 55.995 |
0.49150 |
0.58320 |
| 57.395 |
0.59050 |
0.64220 |
| 57.595 |
0.68000 |
0.69770 |
| 57.862 |
0.75250 |
0.74450 |
| 57.395 |
0.83500 |
0.82050 |
| 57.595 |
0.91950 |
0.90000 |
| 56.662 |
0.92250 |
0.89320 |
(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 |
| Nishi Y.: Vapor-Liquid Equilibria Accompanied by Hypothetical Chemical Reaction. J.Chem.Eng.Japan 5 (1972) 334-339 |
Vapor-Liquid Equilibrium Data Overview
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