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 9082
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
H2O |
18.015 |
7732-18-5 |
Water |
| 2 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
| 3 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
Search the DDB for all data of this mixture
Data Table
| P [kPa] |
T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 98.992 |
366.95 |
0.45300 |
0.46400 |
0.48200 |
0.21400 |
| 100.125 |
371.65 |
0.08160 |
0.72000 |
0.14700 |
0.40500 |
| 100.658 |
368.15 |
0.07240 |
0.64000 |
0.13100 |
0.30400 |
| 99.325 |
366.25 |
0.06500 |
0.61500 |
0.12000 |
0.27400 |
| 98.125 |
363.25 |
0.05500 |
0.55000 |
0.10000 |
0.21900 |
| 97.992 |
362.05 |
0.04770 |
0.51500 |
0.09000 |
0.19000 |
| 98.392 |
360.15 |
0.04100 |
0.45000 |
0.07900 |
0.15100 |
| 101.192 |
359.05 |
0.03460 |
0.39600 |
0.06920 |
0.11400 |
| 100.325 |
356.85 |
0.02600 |
0.32700 |
0.05410 |
0.08250 |
| 100.325 |
355.35 |
0.02290 |
0.26500 |
0.04670 |
0.06310 |
| 100.658 |
354.65 |
0.01630 |
0.22600 |
0.03930 |
0.04710 |
| 100.525 |
353.85 |
0.01400 |
0.19300 |
0.03720 |
0.03610 |
| 97.325 |
352.25 |
0.01160 |
0.16200 |
0.03220 |
0.03220 |
| 100.992 |
373.25 |
0.13400 |
0.72200 |
0.21000 |
0.44800 |
| 100.925 |
366.65 |
0.19190 |
0.59900 |
0.27000 |
0.26300 |
| 100.392 |
362.55 |
0.14900 |
0.53300 |
0.21000 |
0.21200 |
| 101.192 |
374.45 |
0.35000 |
0.60800 |
0.45000 |
0.38000 |
| 100.525 |
367.95 |
0.33300 |
0.55300 |
0.39000 |
0.27600 |
| 100.458 |
363.90 |
0.29000 |
0.51600 |
0.33500 |
0.20600 |
| 100.658 |
361.45 |
0.25800 |
0.48500 |
0.30300 |
0.16300 |
| 100.392 |
359.95 |
0.23100 |
0.46700 |
0.28000 |
0.14200 |
| 99.059 |
356.15 |
0.19600 |
0.30200 |
0.24900 |
0.09210 |
| 97.925 |
354.35 |
0.15950 |
0.34700 |
0.22000 |
0.07200 |
| 99.525 |
354.05 |
0.13400 |
0.31200 |
0.20200 |
0.06000 |
| 97.992 |
352.05 |
0.09300 |
0.24700 |
0.16700 |
0.04040 |
| 97.925 |
351.15 |
0.06590 |
0.19300 |
0.13950 |
0.03000 |
| 101.925 |
350.95 |
0.04540 |
0.15300 |
0.10950 |
0.02190 |
| 101.858 |
371.35 |
0.57500 |
0.39400 |
0.60700 |
0.23100 |
| 101.725 |
366.15 |
0.53200 |
0.39200 |
0.50900 |
0.16600 |
| 100.992 |
369.60 |
0.11200 |
0.66500 |
0.17900 |
0.35600 |
| 100.658 |
366.30 |
0.09380 |
0.60600 |
0.15300 |
0.28600 |
| 99.992 |
364.35 |
0.08300 |
0.57000 |
0.14000 |
0.23700 |
| 99.992 |
363.85 |
0.07390 |
0.55750 |
0.13000 |
0.22400 |
| 98.725 |
359.95 |
0.14000 |
0.49400 |
0.19900 |
0.16400 |
| 98.725 |
359.25 |
0.12200 |
0.46000 |
0.18200 |
0.15500 |
| 98.459 |
357.50 |
0.09860 |
0.41000 |
0.15700 |
0.11700 |
| 98.459 |
357.05 |
0.08350 |
0.39200 |
0.14100 |
0.10800 |
| 97.859 |
355.25 |
0.06250 |
0.33200 |
0.11900 |
0.07460 |
| 97.992 |
354.35 |
0.05000 |
0.28900 |
0.10000 |
0.06150 |
| 99.325 |
353.15 |
0.03430 |
0.21100 |
0.07840 |
0.03940 |
| 99.125 |
352.05 |
0.02400 |
0.15700 |
0.06490 |
0.02360 |
| 99.925 |
372.85 |
0.23400 |
0.67900 |
0.32700 |
0.40000 |
| 99.992 |
369.75 |
0.21200 |
0.64000 |
0.29100 |
0.34100 |
| 101.725 |
360.95 |
0.48400 |
0.37200 |
0.43000 |
0.11300 |
| 100.392 |
355.25 |
0.39800 |
0.32500 |
0.36000 |
0.06925 |
| 100.725 |
351.95 |
0.30900 |
0.26600 |
0.32000 |
0.04350 |
| 100.725 |
350.55 |
0.24550 |
0.22800 |
0.28200 |
0.02720 |
| 99.992 |
349.15 |
0.17000 |
0.17200 |
0.24200 |
0.02450 |
| 99.992 |
348.75 |
0.12550 |
0.13150 |
0.20800 |
0.02050 |
| 100.592 |
348.85 |
0.08700 |
0.11100 |
0.16250 |
0.01690 |
| 100.845 |
376.40 |
0.12600 |
0.76500 |
0.20800 |
0.51700 |
| 100.845 |
365.35 |
0.77610 |
0.19500 |
0.61000 |
0.08900 |
| 99.725 |
372.95 |
0.27980 |
0.63600 |
0.37350 |
0.37400 |
| 99.725 |
357.15 |
0.72250 |
0.19900 |
0.43600 |
0.05500 |
| 101.512 |
371.15 |
0.48980 |
0.46200 |
0.54550 |
0.26000 |
| 102.165 |
351.95 |
0.64750 |
0.18150 |
0.34600 |
0.03100 |
(P - pressure, T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Garner F.H.; Ellis S.R.M.; Pearce C.J.: Extraction of Acetic Acid from Water. Chem.Eng.Sci. 4 (1955) 273-278 |
Vapor-Liquid Equilibrium Data Set 34207
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
H2O |
18.015 |
7732-18-5 |
Water |
| 2 |
C2H4O2 |
60.053 |
64-19-7 |
Acetic acid |
| 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] |
| 350.15 |
0.21660 |
0.15240 |
0.15120 |
0.10000 |
| 349.15 |
0.45940 |
0.21860 |
0.78460 |
0.02197 |
| 357.15 |
0.41530 |
0.23610 |
0.58760 |
0.05560 |
| 347.65 |
0.11000 |
0.29140 |
0.24130 |
0.26930 |
| 346.15 |
0.17700 |
0.13700 |
0.60000 |
0.00000 |
| 344.15 |
0.10950 |
0.17330 |
0.38060 |
0.06290 |
| 348.15 |
0.25960 |
0.18540 |
0.61830 |
0.00630 |
| 344.15 |
0.34430 |
0.12310 |
0.38670 |
0.07620 |
| 346.15 |
0.02770 |
0.13510 |
0.70000 |
0.00000 |
| 357.15 |
0.01430 |
0.14930 |
0.05410 |
0.08930 |
| 356.15 |
0.37980 |
0.13780 |
0.31710 |
0.09880 |
| 342.15 |
0.34680 |
0.11690 |
0.80000 |
0.00000 |
| 369.15 |
0.90230 |
0.01080 |
0.42710 |
0.00726 |
| 370.15 |
0.80700 |
0.18180 |
0.37970 |
0.09280 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Desai S.S.; Gadekar S.V.; Saichandra P.L.V.N.: Vapor Liquid Equilibrium and Residue Curve Map for Acetic Acid-Water-Ethyl Acetate Ternary System. CHEMCON 2010 National Conference (2010) 1-10 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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