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
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
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
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
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
© DDBST GmbH