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 3971

Components

No. Formula Molar Mass CAS Registry Number Name
1 C3H6O 58.080 67-64-1 Acetone
2 C4H8O2 88.106 141-78-6 Ethyl acetate
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]
348.45 0.04600 0.10200
346.95 0.09500 0.19500
345.35 0.14900 0.28850
344.35 0.17150 0.31100
343.35 0.21900 0.38000
341.95 0.26250 0.43700
340.75 0.32750 0.52100
338.25 0.43250 0.61900
336.95 0.50000 0.67800
335.95 0.53750 0.70250
335.35 0.61250 0.76600
333.35 0.72600 0.84500
332.35 0.79500 0.88500
331.25 0.86040 0.92750
330.35 0.91000 0.94800
329.75 0.98000 0.98900

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

Reference

Source
Subrahmanyam V.; Murty P.D.: Vapor-Liquid Equilibria: Systems Acetone Ethyl Acetate Acetone-n-Propyl Acetate. J.Appl.Chem. 14 (1964) 500-502


Vapor-Liquid Equilibrium Data Set 8455

Components

No. Formula Molar Mass CAS Registry Number Name
1 C3H6O 58.080 67-64-1 Acetone
2 C4H8O2 88.106 141-78-6 Ethyl acetate
Search the DDB for all data of this mixture

Constant Value

Pressure 96.93 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
348.05 0.02390 0.06520
347.15 0.05650 0.12230
346.55 0.07610 0.15660
345.35 0.11670 0.22040
343.75 0.16740 0.29840
342.20 0.22450 0.37860
338.80 0.36190 0.54310
337.05 0.44190 0.62460
335.05 0.54180 0.71270
333.35 0.63890 0.78670
331.95 0.72680 0.84550
330.55 0.81680 0.90080
329.80 0.86750 0.92830
329.15 0.91880 0.95520
328.65 0.96110 0.97790
328.36 0.98100 0.98900

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

Reference

Source
Gilburd M.M.; Yurkevich B.P.; Polytanskaya T.I.: Liquid-Vapor Phase Equilibria in Ethyl Acetate-Acetone and Ethyl Acetate Allyl Alcohol Systems. J.Appl.Chem.USSR 52 (1979) 2247-2249


Vapor-Liquid Equilibrium Data Set 10020

Components

No. Formula Molar Mass CAS Registry Number Name
1 C3H6O 58.080 67-64-1 Acetone
2 C4H8O2 88.106 141-78-6 Ethyl acetate
Search the DDB for all data of this mixture

Constant Value

Pressure 53.33 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
332.55 0.00000 0.00000
330.15 0.05690 0.12620
330.05 0.06280 0.13830
328.33 0.11790 0.23770
324.85 0.24970 0.42750
324.75 0.25430 0.43310
323.65 0.30220 0.49000
321.55 0.39780 0.59320
317.55 0.60750 0.77180
315.35 0.73860 0.86010
313.95 0.85280 0.92500
313.75 0.86680 0.93220
312.85 0.94680 0.97260
312.45 1.00000 1.00000

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

Reference

Source
Gilburd M.M.; Politanskaya T.I.; Yurkevich B.P.: Liquid-Vapor Equilibrium in the Systems Ethyl Acetate-Acetone, Acetone-Allyl Alcohol, and Ethyl Acetate-Acetic Acid Under Reduced Pressure. J.Appl.Chem.USSR 54 (1981) 938-940

Diagrams

Vapor-Liquid Equilibrium of Acetone+Ethyl acetate
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Vapor-Liquid Equilibrium of Acetone+Ethyl acetate
See larger image

List of All References

Source
Subrahmanyam V.; Murty P.D.: Vapor-Liquid Equilibria: Systems Acetone Ethyl Acetate Acetone-n-Propyl Acetate. J.Appl.Chem. 14 (1964) 500-502
Gilburd M.M.; Yurkevich B.P.; Polytanskaya T.I.: Liquid-Vapor Phase Equilibria in Ethyl Acetate-Acetone and Ethyl Acetate Allyl Alcohol Systems. J.Appl.Chem.USSR 52 (1979) 2247-2249
Gilburd M.M.; Politanskaya T.I.; Yurkevich B.P.: Liquid-Vapor Equilibrium in the Systems Ethyl Acetate-Acetone, Acetone-Allyl Alcohol, and Ethyl Acetate-Acetic Acid Under Reduced Pressure. J.Appl.Chem.USSR 54 (1981) 938-940

Vapor-Liquid Equilibrium Data Overview


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