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 1130

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O2 88.106 141-78-6 Ethyl acetate
2 H2O 18.015 7732-18-5 Water
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Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
347.25 0.94000 0.84900
347.75 0.95800 0.86900
348.95 0.97600 0.92200

(T - temperature, x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Griswold J.; Chu P.L.; Winsauer W.O.: (Separation of Synthesis Mixtures) Phase Equilibria in Ethyl Alcohol-Ethyl Acetate-Water System. Ind.Eng.Chem. 41 (1949) 2352-2358


Vapor-Liquid Equilibrium Data Set 1131

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O2 88.106 141-78-6 Ethyl acetate
2 H2O 18.015 7732-18-5 Water
Search the DDB for all data of this mixture

Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
347.95 0.97100 0.91400
348.15 0.97400 0.92700
348.75 0.98300 0.94700
349.05 0.98400 0.95300
348.85 0.98600 0.95400

(T - temperature, x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Garner F.H.; Ellis S.R.M.; Pearce C.J.: Extraction of Acetic from Water. Chem.Eng.Sci. 3 (1954) 48-54


Vapor-Liquid Equilibrium Data Set 1132

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O2 88.106 141-78-6 Ethyl acetate
2 H2O 18.015 7732-18-5 Water
Search the DDB for all data of this mixture

Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
372.00 0.00056 0.04055
369.35 0.00114 0.12560
359.65 0.00489 0.59100
349.35 0.00858 0.66800
343.70 0.04590 0.71400
343.60 0.69000 0.70700
343.65 0.77500 0.69900
344.60 0.87370 0.76500
346.50 0.94445 0.86500
348.70 0.98070 0.94110

(T - temperature, x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Ellis S.R.M.; Garbett R.D.: A New Equilibrium Still for the Study of Partially Miscible Systems. Ind.Eng.Chem. Int.Ed. 52 (1960) 385-388

Diagrams

Vapor-Liquid Equilibrium of Ethyl acetate+Water
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Vapor-Liquid Equilibrium of Ethyl acetate+Water
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List of All References

Source
Ellis S.R.M.; Garbett R.D.: A New Equilibrium Still for the Study of Partially Miscible Systems. Ind.Eng.Chem. Int.Ed. 52 (1960) 385-388
Garner F.H.; Ellis S.R.M.; Pearce C.J.: Extraction of Acetic from Water. Chem.Eng.Sci. 3 (1954) 48-54
Griswold J.; Chu P.L.; Winsauer W.O.: (Separation of Synthesis Mixtures) Phase Equilibria in Ethyl Alcohol-Ethyl Acetate-Water System. Ind.Eng.Chem. 41 (1949) 2352-2358

Vapor-Liquid Equilibrium Data Overview


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