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 10966
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
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] |
| 352.75 |
0.06500 |
0.73900 |
0.09600 |
0.83200 |
| 351.65 |
0.13000 |
0.67100 |
0.17100 |
0.76500 |
| 351.15 |
0.19900 |
0.59600 |
0.24200 |
0.69800 |
| 350.55 |
0.27500 |
0.51300 |
0.31000 |
0.63100 |
| 350.65 |
0.35500 |
0.42200 |
0.38200 |
0.56500 |
| 350.05 |
0.43800 |
0.34200 |
0.45600 |
0.48900 |
| 350.65 |
0.52800 |
0.25300 |
0.54300 |
0.40600 |
| 351.45 |
0.61500 |
0.16700 |
0.64200 |
0.30600 |
| 352.85 |
0.69900 |
0.08400 |
0.76800 |
0.17900 |
| 354.85 |
0.05700 |
0.64500 |
0.07800 |
0.82400 |
| 353.95 |
0.11500 |
0.58100 |
0.14500 |
0.76100 |
| 353.45 |
0.17700 |
0.51300 |
0.21000 |
0.70000 |
| 353.35 |
0.24300 |
0.44100 |
0.27700 |
0.63400 |
| 353.45 |
0.38600 |
0.29000 |
0.42500 |
0.49300 |
| 354.35 |
0.45800 |
0.21600 |
0.51000 |
0.40300 |
| 355.35 |
0.53400 |
0.14100 |
0.61600 |
0.29900 |
| 356.45 |
0.61000 |
0.07300 |
0.74100 |
0.17300 |
| 356.75 |
0.05300 |
0.53900 |
0.07000 |
0.79500 |
| 356.25 |
0.10500 |
0.48300 |
0.13200 |
0.73900 |
| 355.85 |
0.15700 |
0.42800 |
0.19500 |
0.67900 |
| 355.85 |
0.21700 |
0.36300 |
0.26100 |
0.61700 |
| 355.95 |
0.27600 |
0.29800 |
0.33000 |
0.54600 |
| 356.75 |
0.34000 |
0.23000 |
0.41800 |
0.48200 |
| 358.95 |
0.46400 |
0.10800 |
0.59900 |
0.26700 |
| 360.35 |
0.52400 |
0.05500 |
0.71900 |
0.14400 |
| 361.05 |
0.08800 |
0.34500 |
0.12300 |
0.68000 |
| 362.65 |
0.09400 |
0.28900 |
0.13800 |
0.64300 |
| 361.05 |
0.12500 |
0.29000 |
0.17700 |
0.62500 |
| 361.65 |
0.12700 |
0.29300 |
0.17800 |
0.62300 |
| 362.05 |
0.17400 |
0.24300 |
0.24500 |
0.55300 |
| 362.65 |
0.22300 |
0.19700 |
0.31800 |
0.47700 |
| 363.15 |
0.27800 |
0.14100 |
0.41200 |
0.38400 |
| 361.75 |
0.35800 |
0.11800 |
0.50400 |
0.31800 |
| 363.15 |
0.38200 |
0.09200 |
0.55500 |
0.25800 |
| 363.85 |
0.40600 |
0.06700 |
0.61000 |
0.20200 |
| 365.95 |
0.45500 |
0.02300 |
0.73100 |
0.07300 |
| 363.25 |
0.01200 |
0.38600 |
0.01800 |
0.75200 |
| 363.85 |
0.02400 |
0.34400 |
0.03500 |
0.73200 |
| 364.45 |
0.03700 |
0.31400 |
0.05400 |
0.70500 |
| 364.85 |
0.05000 |
0.29200 |
0.07500 |
0.68000 |
| 363.75 |
0.11000 |
0.27100 |
0.14900 |
0.63500 |
| 364.35 |
0.14900 |
0.22900 |
0.20600 |
0.57300 |
| 364.85 |
0.16800 |
0.20800 |
0.23700 |
0.54000 |
| 365.35 |
0.18300 |
0.18000 |
0.26800 |
0.49800 |
| 367.25 |
0.21400 |
0.13200 |
0.34600 |
0.39200 |
| 366.35 |
0.22100 |
0.13900 |
0.34000 |
0.41400 |
| 367.65 |
0.23400 |
0.11100 |
0.38000 |
0.35100 |
| 367.85 |
0.25500 |
0.09100 |
0.43000 |
0.24800 |
| 368.45 |
0.28000 |
0.07300 |
0.47800 |
0.24800 |
| 368.75 |
0.30500 |
0.05500 |
0.53300 |
0.19100 |
| 367.95 |
0.04300 |
0.22300 |
0.07400 |
0.64400 |
| 368.35 |
0.05300 |
0.20700 |
0.09000 |
0.59600 |
| 368.85 |
0.06400 |
0.19200 |
0.10900 |
0.57100 |
| 369.25 |
0.07500 |
0.17400 |
0.13200 |
0.54000 |
| 370.05 |
0.08900 |
0.15800 |
0.15800 |
0.50400 |
| 370.45 |
0.13300 |
0.12000 |
0.24300 |
0.41600 |
| 371.65 |
0.14800 |
0.10900 |
0.27300 |
0.37600 |
| 371.25 |
0.14800 |
0.10500 |
0.27200 |
0.38700 |
| 373.05 |
0.16100 |
0.08800 |
0.30500 |
0.34000 |
| 372.95 |
0.17700 |
0.07500 |
0.34100 |
0.29800 |
| 373.25 |
0.22500 |
0.04800 |
0.44400 |
0.19200 |
| 373.85 |
0.23900 |
0.03400 |
0.48400 |
0.14500 |
| 372.95 |
0.01200 |
0.16300 |
0.02200 |
0.59300 |
| 373.35 |
0.02100 |
0.15400 |
0.03800 |
0.56800 |
| 373.85 |
0.02900 |
0.14500 |
0.05500 |
0.54200 |
| 374.85 |
0.03800 |
0.13400 |
0.07200 |
0.51600 |
| 375.35 |
0.04600 |
0.12400 |
0.09000 |
0.48900 |
| 375.35 |
0.05700 |
0.12200 |
0.10900 |
0.47800 |
| 375.95 |
0.07700 |
0.10000 |
0.15300 |
0.42300 |
| 376.75 |
0.08500 |
0.09800 |
0.17300 |
0.39100 |
| 377.25 |
0.09300 |
0.08600 |
0.19300 |
0.35900 |
| 378.55 |
0.11000 |
0.06700 |
0.23600 |
0.29800 |
| 378.15 |
0.12200 |
0.06300 |
0.26500 |
0.26400 |
| 379.15 |
0.13900 |
0.04500 |
0.31500 |
0.20500 |
| 380.15 |
0.14200 |
0.03300 |
0.34100 |
0.15900 |
| 380.75 |
0.15400 |
0.02400 |
0.37200 |
0.12300 |
| 381.85 |
0.16600 |
0.01600 |
0.40800 |
0.08300 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Shono H.; Kanazawa N.; Hashitani M.; Komatsu H.; Hirata M.: Vapor-Liquid Equilibrium in Extractive Distillation of Ethyl Acetate-Ethanol System. Kogyo Kagaku Zasshi 72 (1969) 815-819 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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