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 2220

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H6 54.092 106-99-0 1,3-Butadiene
2 C4H8O2 88.106 141-78-6 Ethyl acetate
Search the DDB for all data of this mixture

Constant Value

Temperature 298.15 K

Data Table

P [kPa] x1 [mol/mol] y1 [mol/mol]
12.615 0.00000 0.00000
28.628 0.05500 0.57600
44.116 0.10910 0.73700
58.446 0.15970 0.81100
71.805 0.20780 0.85400
83.357 0.24980 0.87900
93.806 0.28810 0.89700
103.557 0.32420 0.91100

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

Reference

Source
Wong K.F.; Eckert C.A.: Vapor-Liquid Equilibria of 1,3-Butadiene Systems. J.Chem.Eng.Data 14 (1969) 432-436

Diagrams

Vapor-Liquid Equilibrium of Ethyl acetate+1,3-Butadiene
See larger image
Vapor-Liquid Equilibrium of Ethyl acetate+1,3-Butadiene
See larger image

List of All References

Source
Wong K.F.; Eckert C.A.: Vapor-Liquid Equilibria of 1,3-Butadiene Systems. J.Chem.Eng.Data 14 (1969) 432-436

Vapor-Liquid Equilibrium Data Overview


© DDBST GmbH