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 12971

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O2 88.106 141-78-6 Ethyl acetate
2 C2H6O2 62.068 107-21-1 1,2-Ethanediol
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Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
470.35 0.00000 0.00000
456.45 0.00500 0.36400
447.85 0.00600 0.54600
434.75 0.00800 0.74000
421.85 0.01000 0.88000
413.15 0.01400 0.93600
391.15 0.02600 0.97000
363.65 0.08000 0.97900
357.15 0.12000 0.98500
354.65 0.14400 0.98400
354.55 0.20600 0.98400
354.35 0.22200 0.98400
354.25 0.28300 0.98400
354.15 0.32100 0.98400
353.85 0.40600 0.98400
353.35 0.45700 0.98400
352.85 0.58300 0.98400
351.75 0.78000 0.99000
350.95 0.88500 0.99400
350.55 0.98800 0.99900
350.25 1.00000 1.00000

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

Reference

Source
Thorat R.T.; Nageshwar G.D.: Ethyl Acetate-Ethylene Glycol. Indian Chem.Eng. 30 (1988) 50-54

Diagrams

Vapor-Liquid Equilibrium of 1,2-Ethanediol+Ethyl acetate
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Vapor-Liquid Equilibrium of 1,2-Ethanediol+Ethyl acetate
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List of All References

Source
Thorat R.T.; Nageshwar G.D.: Ethyl Acetate-Ethylene Glycol. Indian Chem.Eng. 30 (1988) 50-54

Vapor-Liquid Equilibrium Data Overview


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