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 12972
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 |
C2H6O2 |
62.068 |
107-21-1 |
1,2-Ethanediol |
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] |
| 351.35 |
0.04710 |
0.84910 |
0.13400 |
0.86050 |
| 350.05 |
0.09360 |
0.79750 |
0.23500 |
0.76290 |
| 349.25 |
0.15010 |
0.74700 |
0.30780 |
0.68760 |
| 348.65 |
0.17810 |
0.70930 |
0.35920 |
0.63770 |
| 348.15 |
0.23600 |
0.65350 |
0.41520 |
0.58160 |
| 347.75 |
0.28710 |
0.60070 |
0.45820 |
0.53920 |
| 347.45 |
0.34960 |
0.54390 |
0.49710 |
0.50180 |
| 347.15 |
0.39220 |
0.50060 |
0.53530 |
0.46350 |
| 346.95 |
0.42080 |
0.47630 |
0.55270 |
0.44640 |
| 346.85 |
0.49110 |
0.40310 |
0.59310 |
0.40340 |
| 346.95 |
0.54990 |
0.33770 |
0.63250 |
0.36290 |
| 347.05 |
0.59910 |
0.28770 |
0.66050 |
0.33700 |
| 346.95 |
0.64950 |
0.24440 |
0.69020 |
0.30720 |
| 348.05 |
0.68500 |
0.12560 |
0.74120 |
0.25350 |
| 348.15 |
0.76190 |
0.02840 |
0.75700 |
0.23190 |
| 350.15 |
0.86650 |
0.03330 |
0.85830 |
0.12860 |
| 349.35 |
0.83510 |
0.06640 |
0.81510 |
0.18350 |
| 354.15 |
0.04390 |
0.66200 |
0.19320 |
0.79760 |
| 353.05 |
0.10250 |
0.57000 |
0.36400 |
0.62880 |
| 352.25 |
0.13020 |
0.54170 |
0.40410 |
0.58920 |
| 351.35 |
0.18620 |
0.49630 |
0.47280 |
0.52080 |
| 350.35 |
0.24570 |
0.45150 |
0.52740 |
0.46690 |
| 349.75 |
0.29760 |
0.40960 |
0.56130 |
0.42440 |
| 349.35 |
0.34770 |
0.36050 |
0.60520 |
0.38160 |
| 349.65 |
0.40270 |
0.30380 |
0.66770 |
0.32380 |
| 349.55 |
0.44730 |
0.26090 |
0.70220 |
0.29040 |
| 349.85 |
0.47060 |
0.21870 |
0.75410 |
0.23740 |
| 350.65 |
0.51040 |
0.16850 |
0.79030 |
0.19720 |
| 356.65 |
0.06520 |
0.42950 |
0.34120 |
0.64720 |
| 354.35 |
0.11150 |
0.39700 |
0.39710 |
0.56970 |
| 352.35 |
0.14060 |
0.36990 |
0.46890 |
0.49600 |
| 352.25 |
0.18120 |
0.32350 |
0.57010 |
0.40740 |
| 351.35 |
0.22810 |
0.28340 |
0.65980 |
0.32810 |
| 351.35 |
0.25240 |
0.25830 |
0.67920 |
0.30620 |
| 351.95 |
0.27750 |
0.21440 |
0.72110 |
0.26370 |
| 351.95 |
0.33320 |
0.16760 |
0.78640 |
0.20180 |
| 368.85 |
0.02410 |
0.15070 |
0.34250 |
0.63440 |
| 362.65 |
0.03750 |
0.16810 |
0.49410 |
0.48480 |
| 358.15 |
0.05820 |
0.19140 |
0.55820 |
0.42900 |
| 356.15 |
0.09210 |
0.20770 |
0.61020 |
0.37150 |
| 353.75 |
0.11350 |
0.19900 |
0.67810 |
0.30920 |
| 354.75 |
0.13270 |
0.16750 |
0.72210 |
0.26820 |
| 354.25 |
0.15010 |
0.15180 |
0.74860 |
0.23260 |
| 353.35 |
0.17820 |
0.12600 |
0.80150 |
0.18130 |
| 392.15 |
0.00190 |
0.07300 |
0.34780 |
0.59990 |
| 375.35 |
0.00720 |
0.11900 |
0.48710 |
0.48080 |
| 367.85 |
0.04450 |
0.08830 |
0.61020 |
0.36730 |
| 360.85 |
0.05920 |
0.09070 |
0.71710 |
0.26080 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Thorat R.T.; Nageshwar G.D.: Ethyl Acetate-Ethanol-Ethylene Glycol. Indian Chem.Eng. 30 (1988) 60-62 |
List of All References
Vapor-Liquid Equilibrium Data Overview
© DDBST GmbH