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 622

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O2 88.106 141-78-6 Ethyl acetate
2 C6H6 78.114 71-43-2 Benzene
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]
353.16 0.01600 0.02000
353.10 0.02700 0.03300
352.92 0.06000 0.07100
352.55 0.13600 0.15700
352.43 0.16000 0.18400
352.11 0.23000 0.25600
351.81 0.30000 0.32900
351.58 0.35900 0.38700
351.34 0.42200 0.44800
351.27 0.44100 0.46500
350.99 0.52800 0.54700
350.82 0.58700 0.60500
350.64 0.69700 0.70700
350.53 0.77400 0.78000
350.47 0.83400 0.83800
350.46 0.84100 0.84500
350.44 0.85700 0.86000
350.38 0.91200 0.91400
350.34 0.95000 0.95100

(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


Vapor-Liquid Equilibrium Data Set 2441

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O2 88.106 141-78-6 Ethyl acetate
2 C6H6 78.114 71-43-2 Benzene
Search the DDB for all data of this mixture

Constant Value

Temperature 323.15 K

Data Table

P [kPa] x1 [mol/mol] y1 [mol/mol]
36.996 0.14970 0.16410
37.509 0.33460 0.35190
37.690 0.45800 0.46960
37.825 0.56970 0.57830
37.940 0.62890 0.63420
37.972 0.67080 0.67460
38.000 0.71700 0.71820
38.053 0.75990 0.76160
38.053 0.76290 0.76460
38.077 0.81620 0.81620
38.102 0.85450 0.85490
38.108 0.86370 0.86370
38.124 0.89760 0.89760

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

Reference

Source
Linek J.; Prochazka K.; Wichterle I.: Liquid-Vapor Equilibrium LIV The Systems Ethyl Acetate-Benzene, Ethyl Acetate-Toluene and Ethyl Acetate-Ethylbenzene. Collect.Czech.Chem.Commun. 37 (1972) 3010-3014


Vapor-Liquid Equilibrium Data Set 2442

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O2 88.106 141-78-6 Ethyl acetate
2 C6H6 78.114 71-43-2 Benzene
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]
53.298 0.12250 0.14220
54.642 0.31240 0.33020
55.046 0.39040 0.40790
55.381 0.47240 0.49000
55.645 0.57020 0.58220
55.769 0.63380 0.64280
55.862 0.68410 0.69080
55.943 0.75950 0.76460
55.985 0.82000 0.82050

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

Reference

Source
Linek J.; Prochazka K.; Wichterle I.: Liquid-Vapor Equilibrium LIV The Systems Ethyl Acetate-Benzene, Ethyl Acetate-Toluene and Ethyl Acetate-Ethylbenzene. Collect.Czech.Chem.Commun. 37 (1972) 3010-3014

Diagrams

Vapor-Liquid Equilibrium of Ethyl acetate+Benzene
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Vapor-Liquid Equilibrium of Ethyl acetate+Benzene
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Vapor-Liquid Equilibrium of Ethyl acetate+Benzene
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Vapor-Liquid Equilibrium of Ethyl acetate+Benzene
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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
Linek J.; Prochazka K.; Wichterle I.: Liquid-Vapor Equilibrium LIV The Systems Ethyl Acetate-Benzene, Ethyl Acetate-Toluene and Ethyl Acetate-Ethylbenzene. Collect.Czech.Chem.Commun. 37 (1972) 3010-3014

Vapor-Liquid Equilibrium Data Overview


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