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 459

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O2 88.106 141-78-6 Ethyl acetate
2 C3H8O 60.096 67-63-0 2-Propanol
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Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
354.15 0.10000 0.16580
351.95 0.20000 0.28890
350.55 0.30000 0.38760
349.55 0.40000 0.48060
349.35 0.50000 0.54980
349.15 0.60000 0.62680
349.55 0.70000 0.70660
348.65 0.80000 0.78360
349.75 0.90000 0.88540

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

Reference

Source
Nishi Y.: Vapor-Liquid Equilibria Accompanied by Hypothetical Chemical Reaction. J.Chem.Eng.Japan 5 (1972) 334-339


Vapor-Liquid Equilibrium Data Set 609

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O2 88.106 141-78-6 Ethyl acetate
2 C3H8O 60.096 67-63-0 2-Propanol
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Constant Value

Temperature 313.15 K

Data Table

P [kPa] x1 [mol/mol] y1 [mol/mol]
15.732 0.03800 0.13470
16.065 0.05000 0.16600
16.799 0.07000 0.21750
18.265 0.11550 0.30650
19.798 0.15000 0.37300
20.332 0.19900 0.42300
21.532 0.27000 0.49500
21.865 0.29000 0.50400
23.198 0.38500 0.57800
23.731 0.46150 0.62250
24.465 0.54000 0.66650
25.465 0.64050 0.71200
25.865 0.81400 0.81500
25.598 0.90850 0.89860

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

Reference

Source
Murti P.S.; van Winkle M.: Vapor-Liquid Equilibria for Binary Systems of Methanol, Ethyl Alcohol, 1-Propanol, and 2-Propanol with Ethyl Acetate and 1-Propanol-Water. Ind.Eng.Chem. Chem.Eng.Data Series 3 (1958) 72-81


Vapor-Liquid Equilibrium Data Set 610

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O2 88.106 141-78-6 Ethyl acetate
2 C3H8O 60.096 67-63-0 2-Propanol
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]
41.663 0.04550 0.12540
42.863 0.07400 0.15850
43.930 0.08550 0.19000
44.063 0.09350 0.21760
45.730 0.12950 0.26280
47.329 0.15900 0.29800
47.796 0.17550 0.32050
51.329 0.26650 0.42130
52.529 0.31350 0.46130
53.929 0.36000 0.48810
54.862 0.42750 0.53690
55.062 0.43200 0.54130
55.995 0.49150 0.58320
57.395 0.59050 0.64220
57.595 0.68000 0.69770
57.862 0.75250 0.74450
57.395 0.83500 0.82050
57.595 0.91950 0.90000
56.662 0.92250 0.89320

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

Reference

Source
Murti P.S.; van Winkle M.: Vapor-Liquid Equilibria for Binary Systems of Methanol, Ethyl Alcohol, 1-Propanol, and 2-Propanol with Ethyl Acetate and 1-Propanol-Water. Ind.Eng.Chem. Chem.Eng.Data Series 3 (1958) 72-81

Diagrams

Vapor-Liquid Equilibrium of Ethyl acetate+2-Propanol
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Vapor-Liquid Equilibrium of Ethyl acetate+2-Propanol
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Vapor-Liquid Equilibrium of Ethyl acetate+2-Propanol
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Vapor-Liquid Equilibrium of Ethyl acetate+2-Propanol
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List of All References

Source
Murti P.S.; van Winkle M.: Vapor-Liquid Equilibria for Binary Systems of Methanol, Ethyl Alcohol, 1-Propanol, and 2-Propanol with Ethyl Acetate and 1-Propanol-Water. Ind.Eng.Chem. Chem.Eng.Data Series 3 (1958) 72-81
Nishi Y.: Vapor-Liquid Equilibria Accompanied by Hypothetical Chemical Reaction. J.Chem.Eng.Japan 5 (1972) 334-339

Vapor-Liquid Equilibrium Data Overview


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