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 15816
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 |
| 4 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
x3 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
y3 [mol/mol] |
| 339.25 |
0.19900 |
0.32000 |
0.19200 |
0.34300 |
0.29100 |
0.16600 |
| 339.45 |
0.19900 |
0.32000 |
0.38400 |
0.34900 |
0.26700 |
0.29300 |
| 340.05 |
0.19900 |
0.64200 |
0.03200 |
0.34600 |
0.39600 |
0.04700 |
| 339.95 |
0.19900 |
0.64300 |
0.09600 |
0.35100 |
0.37400 |
0.14900 |
| 339.35 |
0.20000 |
0.16000 |
0.12700 |
0.41500 |
0.27300 |
0.11700 |
| 339.95 |
0.20000 |
0.16000 |
0.25600 |
0.37300 |
0.22800 |
0.21200 |
| 339.45 |
0.20000 |
0.32000 |
0.09600 |
0.38300 |
0.33800 |
0.08800 |
| 340.85 |
0.20000 |
0.32100 |
0.28800 |
0.34700 |
0.27100 |
0.22700 |
| 339.85 |
0.20000 |
0.42400 |
0.25600 |
0.36700 |
0.37100 |
0.16400 |
| 339.45 |
0.20000 |
0.48200 |
0.06300 |
0.35800 |
0.34300 |
0.06900 |
| 340.25 |
0.20000 |
0.64400 |
0.06200 |
0.36400 |
0.42200 |
0.07800 |
| 340.55 |
0.20100 |
0.16000 |
0.38400 |
0.36000 |
0.19800 |
0.29000 |
| 339.25 |
0.20100 |
0.48200 |
0.19000 |
0.34100 |
0.33200 |
0.18900 |
| 339.55 |
0.20100 |
0.48400 |
0.12600 |
0.34500 |
0.36500 |
0.12100 |
| 340.45 |
0.20100 |
0.64700 |
0.12600 |
0.34800 |
0.37200 |
0.15700 |
| 339.85 |
0.30000 |
0.16000 |
0.51300 |
0.34200 |
0.19100 |
0.36500 |
| 337.15 |
0.38800 |
0.46500 |
0.09000 |
0.48700 |
0.29100 |
0.10500 |
| 335.85 |
0.39800 |
0.11900 |
0.38300 |
0.51400 |
0.12200 |
0.28100 |
| 336.55 |
0.39800 |
0.47800 |
0.07200 |
0.49800 |
0.30600 |
0.08300 |
| 335.95 |
0.40000 |
0.12000 |
0.09600 |
0.59500 |
0.18900 |
0.07500 |
| 336.05 |
0.40000 |
0.12000 |
0.19200 |
0.50100 |
0.12400 |
0.12400 |
| 336.15 |
0.40000 |
0.12000 |
0.28900 |
0.57200 |
0.11900 |
0.20700 |
| 336.15 |
0.40000 |
0.24000 |
0.14400 |
0.52700 |
0.20000 |
0.13200 |
| 336.45 |
0.40000 |
0.36100 |
0.14400 |
0.49000 |
0.25500 |
0.14000 |
| 333.95 |
0.40100 |
0.24000 |
0.07200 |
0.55800 |
0.22100 |
0.06200 |
| 336.35 |
0.40100 |
0.24200 |
0.21500 |
0.58500 |
0.08200 |
0.20900 |
| 336.35 |
0.40100 |
0.36200 |
0.09800 |
0.50900 |
0.25300 |
0.09700 |
| 337.35 |
0.40100 |
0.48000 |
0.02400 |
0.48600 |
0.33400 |
0.03400 |
| 336.85 |
0.40100 |
0.48200 |
0.04700 |
0.52700 |
0.31400 |
0.05800 |
| 336.15 |
0.40700 |
0.23800 |
0.28600 |
0.47700 |
0.20100 |
0.23300 |
| 336.25 |
0.40900 |
0.34700 |
0.04800 |
0.54900 |
0.26600 |
0.04700 |
| 333.15 |
0.59800 |
0.15900 |
0.19200 |
0.65000 |
0.11800 |
0.17000 |
| 333.75 |
0.60000 |
0.23900 |
0.06300 |
0.65600 |
0.16900 |
0.06500 |
| 333.75 |
0.60000 |
0.31900 |
0.04700 |
0.67900 |
0.21100 |
0.05100 |
| 333.05 |
0.60100 |
0.08000 |
0.12800 |
0.70500 |
0.08500 |
0.10900 |
| 333.45 |
0.60200 |
0.16000 |
0.04800 |
0.66600 |
0.14500 |
0.05300 |
| 333.55 |
0.60200 |
0.16100 |
0.09600 |
0.70500 |
0.12200 |
0.07900 |
| 333.85 |
0.60200 |
0.24000 |
0.09500 |
0.65000 |
0.18200 |
0.09800 |
| 334.15 |
0.60200 |
0.32100 |
0.03100 |
0.64300 |
0.25000 |
0.04000 |
| 332.85 |
0.60300 |
0.07900 |
0.06300 |
0.77700 |
0.02700 |
0.06700 |
| 333.15 |
0.60300 |
0.07900 |
0.19200 |
0.67000 |
0.16500 |
0.06400 |
| 333.55 |
0.60300 |
0.16000 |
0.14400 |
0.67200 |
0.12700 |
0.11900 |
| 332.95 |
0.60400 |
0.07900 |
0.25600 |
0.65600 |
0.06600 |
0.19700 |
| 333.95 |
0.60400 |
0.24100 |
0.12600 |
0.64000 |
0.16900 |
0.14500 |
| 333.95 |
0.60400 |
0.32100 |
0.01300 |
0.67800 |
0.20600 |
0.02300 |
| 333.55 |
0.60500 |
0.24100 |
0.03000 |
0.68800 |
0.18700 |
0.03300 |
| 334.35 |
0.60500 |
0.32200 |
0.06100 |
0.66900 |
0.19300 |
0.08400 |
| 331.75 |
0.77000 |
0.14300 |
0.05500 |
0.72100 |
0.11000 |
0.07000 |
| 330.95 |
0.79600 |
0.08000 |
0.09500 |
0.78900 |
0.06500 |
0.09000 |
| 331.65 |
0.79700 |
0.11900 |
0.06300 |
0.81700 |
0.07700 |
0.06800 |
| 330.75 |
0.79900 |
0.03900 |
0.12800 |
0.81800 |
0.02400 |
0.11400 |
| 331.55 |
0.80000 |
0.16000 |
0.01600 |
0.81800 |
0.11000 |
0.02700 |
| 330.95 |
0.80100 |
0.04000 |
0.09600 |
0.71100 |
0.01800 |
0.17700 |
| 331.65 |
0.80100 |
0.16000 |
0.00800 |
0.82600 |
0.10100 |
0.01400 |
| 331.05 |
0.80200 |
0.03900 |
0.06400 |
0.82700 |
0.03100 |
0.06300 |
| 331.05 |
0.80200 |
0.04000 |
0.03100 |
0.85100 |
0.02100 |
0.02500 |
| 331.35 |
0.80200 |
0.12000 |
0.01500 |
0.83000 |
0.08400 |
0.01900 |
| 330.95 |
0.80300 |
0.07900 |
0.02300 |
0.84900 |
0.05600 |
0.00600 |
| 331.15 |
0.80300 |
0.07900 |
0.07100 |
0.81600 |
0.06200 |
0.06600 |
| 331.15 |
0.80300 |
0.16100 |
0.02400 |
0.69500 |
0.08800 |
0.18400 |
| 331.05 |
0.80600 |
0.07900 |
0.04500 |
0.81700 |
0.06400 |
0.05700 |
| 331.35 |
0.80800 |
0.12000 |
0.03000 |
0.84500 |
0.06200 |
0.03400 |
| 331.55 |
0.81800 |
0.14200 |
0.03000 |
0.83800 |
0.09200 |
0.04000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Rogova N.B.; Garber Y.N.; Ushakova M.V.; Leonteva S.Yu.: Untersuchung des Dampf-Flüssig-Gleichgewichtes im System Aceton-Ethylacetat-Ethanol-Wasser. Gidrodin.Yavl.Peren.Dvukh.Disp.Sist. (1984) 73-76 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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