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 627

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O2 88.106 141-78-6 Ethyl acetate
2 C8H10 106.167 106-42-3 p-Xylene
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]
409.69 0.00600 0.04800
406.27 0.01900 0.13800
403.18 0.03300 0.22000
401.03 0.04400 0.28000
396.59 0.07000 0.38400
392.23 0.10000 0.47500
389.12 0.12400 0.53000
384.28 0.16500 0.61200
378.20 0.23500 0.69500
372.77 0.31000 0.77100
368.15 0.39900 0.82500
366.32 0.44000 0.84700
363.27 0.52400 0.87800
359.69 0.63500 0.91600
358.80 0.66700 0.92500
356.25 0.76500 0.94800
354.06 0.84600 0.96700
352.35 0.91200 0.98100
351.32 0.94900 0.98900
351.07 0.96500 0.99200

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

Reference

Source
Carr A.D.; Kropholler H.W.: Vapor-Liquid Equilibria at Atmospheric Pressure. J.Chem.Eng.Data 7 (1962) 26-28

Diagrams

Vapor-Liquid Equilibrium of Ethyl acetate+p-Xylene
See larger image 		Vapor-Liquid Equilibrium of Ethyl acetate+p-Xylene
See larger image

List of All References

Source
Carr A.D.; Kropholler H.W.: Vapor-Liquid Equilibria at Atmospheric Pressure. J.Chem.Eng.Data 7 (1962) 26-28

Vapor-Liquid Equilibrium Data Overview

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