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 10968
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 2 |
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] |
y1 [mol/mol] |
| 394.95 |
0.03900 |
0.14100 |
| 390.35 |
0.09600 |
0.29900 |
| 384.05 |
0.17200 |
0.47100 |
| 376.45 |
0.29100 |
0.63900 |
| 370.15 |
0.40600 |
0.74200 |
| 366.85 |
0.47900 |
0.80700 |
| 364.55 |
0.55200 |
0.83800 |
| 362.65 |
0.57800 |
0.86400 |
| 359.45 |
0.68900 |
0.90300 |
| 355.55 |
0.80700 |
0.94900 |
| 352.35 |
0.90400 |
0.97800 |
| 352.15 |
0.91400 |
0.98000 |
| 350.75 |
0.95600 |
0.99000 |
(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 |
Vapor-Liquid Equilibrium Data Set 34586
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 2 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 19.170 |
350.12 |
0.00000 |
0.00000 |
| 23.360 |
350.07 |
0.05300 |
0.22100 |
| 26.720 |
350.03 |
0.09400 |
0.34600 |
| 30.070 |
350.06 |
0.13800 |
0.44900 |
| 33.110 |
350.07 |
0.17600 |
0.51800 |
| 36.830 |
350.12 |
0.22200 |
0.59400 |
| 40.480 |
350.05 |
0.26500 |
0.64800 |
| 44.000 |
350.11 |
0.31300 |
0.69700 |
| 47.330 |
350.14 |
0.34900 |
0.73000 |
| 50.030 |
350.12 |
0.38200 |
0.75500 |
| 54.380 |
350.11 |
0.43400 |
0.79500 |
| 58.260 |
350.10 |
0.47600 |
0.82200 |
| 62.190 |
350.08 |
0.51900 |
0.85000 |
| 67.800 |
350.04 |
0.59900 |
0.88200 |
| 72.600 |
350.10 |
0.65800 |
0.90500 |
| 77.090 |
350.06 |
0.71500 |
0.92600 |
| 82.250 |
350.08 |
0.77700 |
0.94500 |
| 85.950 |
350.12 |
0.81900 |
0.95700 |
| 90.330 |
350.11 |
0.87300 |
0.97100 |
| 94.870 |
350.05 |
0.93100 |
0.98500 |
| 99.460 |
350.06 |
0.98500 |
0.99700 |
| 100.680 |
350.02 |
1.00000 |
1.00000 |
(P - pressure, T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Laavi H.; Pokki J.-P.; Uusi-Kyyny P.; Massimi A.; Kim Y.; Sapei E.; Alopaeus V.: Vapor–Liquid Equilibrium at 350 K, Excess Molar Enthalpies at 298 K, and Excess Molar Volumes at 298 K of Binary Mixtures Containing Ethyl Acetate, Butyl Acetate, and 2-Butanol. J.Chem.Eng.Data 58 (2013) 1011-1019 |
Diagrams
List of All References
| 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 |
| Laavi H.; Pokki J.-P.; Uusi-Kyyny P.; Massimi A.; Kim Y.; Sapei E.; Alopaeus V.: Vapor–Liquid Equilibrium at 350 K, Excess Molar Enthalpies at 298 K, and Excess Molar Volumes at 298 K of Binary Mixtures Containing Ethyl Acetate, Butyl Acetate, and 2-Butanol. J.Chem.Eng.Data 58 (2013) 1011-1019 |
Vapor-Liquid Equilibrium Data Overview
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