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 8029

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H12 84.161 592-41-6 1-Hexene
2 C4H8O2 88.106 141-78-6 Ethyl acetate
Search the DDB for all data of this mixture

Constant Value

Temperature 333.15 K

Data Table

P [kPa] x1 [mol/mol] y1 [mol/mol]
56.075 0.00000 0.00000
58.241 0.01810 0.05360
60.195 0.03320 0.09350
62.430 0.05450 0.14310
64.195 0.07250 0.18130
67.294 0.10620 0.24240
69.940 0.13780 0.29150
72.894 0.17680 0.34380
75.744 0.22110 0.39450
79.013 0.27780 0.44630
81.084 0.32010 0.48610
83.193 0.37220 0.52670
85.193 0.42710 0.56550
86.913 0.48520 0.60420
88.878 0.56320 0.65420
90.253 0.61980 0.68960
91.258 0.68020 0.72830
91.952 0.73670 0.76630
92.532 0.79950 0.81110
92.652 0.84990 0.85040
92.438 0.89230 0.88670
92.112 0.93300 0.92540
91.663 0.97570 0.97130
91.392 1.00000 1.00000

(P - pressure, x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Gmehling J.: Isothermal Vapor-Liquid Equilibria in Binary Systems Formed by Esters with Alkenes. J.Chem.Eng.Data 28 (1983) 27-30

Diagrams

Vapor-Liquid Equilibrium of Ethyl acetate+1-Hexene
See larger image 		Vapor-Liquid Equilibrium of Ethyl acetate+1-Hexene
See larger image

List of All References

Source
Gmehling J.: Isothermal Vapor-Liquid Equilibria in Binary Systems Formed by Esters with Alkenes. J.Chem.Eng.Data 28 (1983) 27-30

Vapor-Liquid Equilibrium Data Overview

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