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 12039
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 |
| 3 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 333.45 |
0.66900 |
0.14400 |
0.75000 |
0.10300 |
| 334.05 |
0.58200 |
0.16800 |
0.68500 |
0.12300 |
| 334.25 |
0.59600 |
0.17100 |
0.70200 |
0.12600 |
| 334.65 |
0.58700 |
0.26000 |
0.68400 |
0.19000 |
| 334.95 |
0.56900 |
0.22900 |
0.66600 |
0.17100 |
| 335.45 |
0.54500 |
0.04100 |
0.67300 |
0.03300 |
| 336.25 |
0.45200 |
0.23300 |
0.57800 |
0.18100 |
| 336.65 |
0.49100 |
0.38900 |
0.58900 |
0.29400 |
| 337.05 |
0.42800 |
0.30000 |
0.51400 |
0.24800 |
| 337.25 |
0.42000 |
0.02400 |
0.60300 |
0.02500 |
| 337.65 |
0.39000 |
0.16200 |
0.51100 |
0.15000 |
| 338.05 |
0.32900 |
0.35800 |
0.47000 |
0.28500 |
| 338.25 |
0.34500 |
0.26400 |
0.44600 |
0.23300 |
| 338.95 |
0.37700 |
0.51300 |
0.49600 |
0.38100 |
| 339.05 |
0.28900 |
0.42600 |
0.41200 |
0.33700 |
| 339.25 |
0.29500 |
0.27700 |
0.40800 |
0.25500 |
| 339.35 |
0.35500 |
0.05400 |
0.50400 |
0.05700 |
| 339.45 |
0.34600 |
0.09000 |
0.47400 |
0.09800 |
| 339.55 |
0.26700 |
0.32700 |
0.38100 |
0.29000 |
| 340.75 |
0.19700 |
0.43900 |
0.28200 |
0.38000 |
| 340.75 |
0.24200 |
0.56400 |
0.35600 |
0.44700 |
| 340.75 |
0.30300 |
0.61200 |
0.41800 |
0.47900 |
| 341.05 |
0.22300 |
0.17200 |
0.33600 |
0.18300 |
| 341.35 |
0.16400 |
0.41700 |
0.23900 |
0.38300 |
| 341.55 |
0.18500 |
0.63100 |
0.27600 |
0.51800 |
| 341.55 |
0.23900 |
0.03700 |
0.39300 |
0.04600 |
| 341.65 |
0.15200 |
0.35100 |
0.23800 |
0.33600 |
| 342.25 |
0.19900 |
0.18600 |
0.29200 |
0.20900 |
| 342.35 |
0.11500 |
0.51300 |
0.18300 |
0.46200 |
| 342.75 |
0.17100 |
0.67900 |
0.24800 |
0.56600 |
| 342.75 |
0.18300 |
0.12000 |
0.29300 |
0.13800 |
| 342.85 |
0.11100 |
0.62600 |
0.16700 |
0.55000 |
| 343.05 |
0.15700 |
0.13600 |
0.25300 |
0.16100 |
| 343.05 |
0.18700 |
0.05000 |
0.31300 |
0.07300 |
| 343.25 |
0.22800 |
0.76200 |
0.34100 |
0.63200 |
| 343.35 |
0.06900 |
0.46700 |
0.10700 |
0.46400 |
| 343.35 |
0.07400 |
0.40900 |
0.11800 |
0.40600 |
| 343.35 |
0.13300 |
0.73300 |
0.20400 |
0.62600 |
| 343.45 |
0.07500 |
0.34900 |
0.12100 |
0.38500 |
| 343.45 |
0.09100 |
0.26500 |
0.14900 |
0.29500 |
| 343.45 |
0.09500 |
0.27100 |
0.14600 |
0.30300 |
| 343.85 |
0.17100 |
0.08200 |
0.28300 |
0.10100 |
| 344.05 |
0.12600 |
0.11700 |
0.21100 |
0.15000 |
| 344.15 |
0.07400 |
0.22500 |
0.12900 |
0.26600 |
| 344.25 |
0.06600 |
0.72000 |
0.10600 |
0.62800 |
| 344.95 |
0.05500 |
0.18200 |
0.10300 |
0.23800 |
| 345.35 |
0.11600 |
0.08000 |
0.20400 |
0.11100 |
| 345.45 |
0.06000 |
0.14000 |
0.12000 |
0.18700 |
| 345.55 |
0.08300 |
0.82800 |
0.13500 |
0.74600 |
| 345.85 |
0.01200 |
0.29100 |
0.02600 |
0.34400 |
| 346.25 |
0.03400 |
0.20700 |
0.03800 |
0.26500 |
| 346.65 |
0.05700 |
0.88600 |
0.09400 |
0.81600 |
| 346.75 |
0.09600 |
0.05100 |
0.18400 |
0.07400 |
| 347.95 |
0.02100 |
0.12400 |
0.03200 |
0.18600 |
| 348.55 |
0.05100 |
0.02900 |
0.11400 |
0.05100 |
| 349.15 |
0.00400 |
0.07400 |
0.01600 |
0.11900 |
| 349.95 |
0.02000 |
0.01100 |
0.05600 |
0.02200 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Carta R.; Dernini S.; Sanna P.: Isobaric Vapor Liquid Equilibria for the Ternary System Acetone - Ethyl Acetate - Ethanol. J.Chem.Eng.Data 29 (1984) 463-466 |
Vapor-Liquid Equilibrium Data Set 14691
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
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] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 343.15 |
0.17540 |
0.20690 |
0.25120 |
0.24390 |
| 339.95 |
0.31920 |
0.16910 |
0.41350 |
0.17900 |
| 336.65 |
0.48720 |
0.12240 |
0.62880 |
0.10730 |
| 333.55 |
0.71270 |
0.06380 |
0.79930 |
0.05860 |
| 343.15 |
0.09760 |
0.40520 |
0.16230 |
0.39740 |
| 339.45 |
0.27020 |
0.34410 |
0.40760 |
0.28130 |
| 334.25 |
0.46580 |
0.23820 |
0.58030 |
0.20370 |
| 333.65 |
0.67370 |
0.14150 |
0.74170 |
0.13140 |
| 343.35 |
0.09370 |
0.60400 |
0.17310 |
0.51860 |
| 339.25 |
0.26340 |
0.49730 |
0.40230 |
0.39040 |
| 336.05 |
0.45020 |
0.37950 |
0.59200 |
0.26100 |
| 333.55 |
0.62950 |
0.23720 |
0.77860 |
0.14280 |
| 344.35 |
0.09350 |
0.75950 |
0.18210 |
0.62550 |
| 339.45 |
0.27700 |
0.60740 |
0.41720 |
0.45990 |
| 335.95 |
0.43650 |
0.47710 |
0.58260 |
0.33640 |
| 333.15 |
0.63110 |
0.30640 |
0.73520 |
0.22260 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Rogova N.B.; Garber Yu.N.; Polyakova L.V.; Andreeva N.G.: Recovery of Acetone, Ethanol and Ethyl Acetate from Aqueous Solutions. J.Appl.Chem.USSR 59 (1986) 1435-1441 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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