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 4888

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H12O2 116.160 123-86-4 Acetic acid butyl ester
2 C2H6O2 62.068 107-21-1 1,2-Ethanediol
Search the DDB for all data of this mixture

Constant Value

Pressure 96.66 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
468.85 0.00000 0.00000
462.05 0.00380 0.19130
448.15 0.01330 0.47160
427.55 0.04000 0.74450
422.35 0.05150 0.79000
407.15 0.12470 0.88300
405.35 0.18490 0.88600
404.45 0.31710 0.88900
404.45 0.42870 0.88900
404.45 0.51590 0.88900
404.45 0.52740 0.88900
403.95 0.66620 0.90200
403.65 0.68980 0.90600
403.25 0.73450 0.91450
401.65 0.83050 0.93500
400.55 0.87400 0.94600
399.75 0.92080 0.96200
399.15 0.94840 0.97400
397.85 1.00000 1.00000

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

Reference

Source
Mainkar S.V.; Mene P.S.: Binary Vapour Liquid Equilibria for n-Butanol Ethylene Glycol & n-Butyl Acetate-Ethylene Glycol Systems. Indian J.Technol. 8 (1970) 320-322

Diagrams

Vapor-Liquid Equilibrium of 1,2-Ethanediol+Acetic acid butyl ester
See larger image 		Vapor-Liquid Equilibrium of 1,2-Ethanediol+Acetic acid butyl ester
See larger image

List of All References

Source
Mainkar S.V.; Mene P.S.: Binary Vapour Liquid Equilibria for n-Butanol Ethylene Glycol & n-Butyl Acetate-Ethylene Glycol Systems. Indian J.Technol. 8 (1970) 320-322

Vapor-Liquid Equilibrium Data Overview

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