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 8209
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
| 29.490 |
0.00000 |
1.00000 |
| 35.338 |
0.05400 |
0.63950 |
| 41.030 |
0.10890 |
0.60240 |
| 45.962 |
0.16240 |
0.56620 |
| 50.260 |
0.21540 |
0.53040 |
| 53.648 |
0.26180 |
0.49900 |
| 56.711 |
0.30870 |
0.46740 |
| 59.508 |
0.35650 |
0.43500 |
| 62.054 |
0.40450 |
0.40260 |
| 64.469 |
0.45460 |
0.36870 |
| 66.721 |
0.50530 |
0.33440 |
| 34.806 |
0.05440 |
0.28760 |
| 41.718 |
0.10800 |
0.27130 |
| 47.295 |
0.16040 |
0.25540 |
| 51.886 |
0.21270 |
0.23950 |
| 58.900 |
0.31410 |
0.20870 |
| 61.607 |
0.36270 |
0.19390 |
| 64.067 |
0.41260 |
0.17880 |
| 66.195 |
0.46100 |
0.16400 |
| 72.569 |
0.62250 |
0.05740 |
| 71.091 |
0.59020 |
0.10650 |
| 69.588 |
0.55810 |
0.15510 |
| 68.060 |
0.52580 |
0.20400 |
| 66.472 |
0.49380 |
0.25250 |
| 64.949 |
0.46190 |
0.30070 |
| 63.165 |
0.42710 |
0.35350 |
| 61.442 |
0.39450 |
0.40280 |
| 59.756 |
0.36250 |
0.45130 |
| 57.986 |
0.33060 |
0.49960 |
| 12.331 |
0.00000 |
0.00000 |
| 62.259 |
0.27760 |
0.05240 |
| 59.074 |
0.26270 |
0.10370 |
| 56.495 |
0.24870 |
0.15190 |
| 54.196 |
0.23440 |
0.20100 |
| 52.166 |
0.22000 |
0.25020 |
| 50.313 |
0.20520 |
0.30080 |
| 48.660 |
0.19080 |
0.34990 |
| 47.095 |
0.17590 |
0.40110 |
| 45.648 |
0.16090 |
0.45220 |
| 44.291 |
0.14610 |
0.50260 |
| 55.299 |
0.28260 |
0.66870 |
| 54.238 |
0.26770 |
0.63340 |
| 53.077 |
0.25250 |
0.59750 |
| 51.945 |
0.23780 |
0.56280 |
| 50.761 |
0.22280 |
0.52720 |
| 49.515 |
0.20680 |
0.48930 |
| 48.347 |
0.19200 |
0.45430 |
| 47.244 |
0.17730 |
0.41940 |
| 46.120 |
0.16240 |
0.38410 |
| 45.051 |
0.14780 |
0.34970 |
| 82.000 |
1.00000 |
0.00000 |
| 70.094 |
0.58960 |
0.25150 |
| 68.862 |
0.55260 |
0.23570 |
| 67.732 |
0.51950 |
0.22160 |
| 66.561 |
0.48480 |
0.20680 |
| 65.377 |
0.45000 |
0.19200 |
| 64.212 |
0.41580 |
0.17740 |
| 63.053 |
0.38090 |
0.16250 |
| 61.875 |
0.34630 |
0.14780 |
| 68.160 |
0.50980 |
0.14920 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Chaudhry M.M.; van Ness H.C.; Abbott M.M.: 6. Total-Pressure Data and GE for Acetone-Ethanol-Water at 50°C. J.Chem.Eng.Data 25 (1980) 254-257 |
Vapor-Liquid Equilibrium Data Set 27935
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 21.145 |
0.10000 |
0.10000 |
0.69700 |
0.12500 |
| 18.425 |
0.10000 |
0.30000 |
0.57000 |
0.25400 |
| 18.052 |
0.10000 |
0.50000 |
0.50000 |
0.34400 |
| 17.705 |
0.10000 |
0.70000 |
0.45600 |
0.43700 |
| 25.318 |
0.20000 |
0.10000 |
0.77500 |
0.08600 |
| 23.225 |
0.20000 |
0.30000 |
0.67900 |
0.18700 |
| 22.425 |
0.20000 |
0.50000 |
0.62500 |
0.26500 |
| 21.878 |
0.20000 |
0.70000 |
0.59700 |
0.35000 |
| 26.958 |
0.30000 |
0.20000 |
0.76200 |
0.11900 |
| 26.145 |
0.30000 |
0.40000 |
0.70500 |
0.19600 |
| 25.011 |
0.30000 |
0.60000 |
0.67900 |
0.27300 |
| 29.184 |
0.40000 |
0.20000 |
0.78800 |
0.10700 |
| 27.944 |
0.40000 |
0.40000 |
0.74300 |
0.18200 |
| 31.251 |
0.50000 |
0.10000 |
0.84200 |
0.05700 |
| 29.998 |
0.50000 |
0.30000 |
0.78800 |
0.13900 |
| 32.331 |
0.60000 |
0.10000 |
0.85600 |
0.05300 |
| 33.544 |
0.70000 |
0.20000 |
0.85500 |
0.09700 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| D'Avila S.G.; Cotrim M.L.: Prediction of Isothermal Vapor Liquid Equilibrium Data of Non Ideal Ternary Mixtures from Binary Data System: Acetone-Ethanol-Water. Rev.Bras.Tecnol. 4 (1973) 191-197 |
Vapor-Liquid Equilibrium Data Set 27936
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 27.184 |
0.10000 |
0.10000 |
0.69200 |
0.12600 |
| 25.051 |
0.10000 |
0.30000 |
0.56100 |
0.25900 |
| 23.051 |
0.10000 |
0.50000 |
0.49000 |
0.34800 |
| 22.265 |
0.10000 |
0.70000 |
0.45000 |
0.43500 |
| 32.717 |
0.20000 |
0.10000 |
0.76400 |
0.09000 |
| 30.118 |
0.20000 |
0.30000 |
0.66400 |
0.19600 |
| 28.238 |
0.20000 |
0.50000 |
0.61000 |
0.27200 |
| 27.624 |
0.20000 |
0.70000 |
0.58600 |
0.35400 |
| 33.717 |
0.30000 |
0.20000 |
0.74600 |
0.12700 |
| 31.971 |
0.30000 |
0.40000 |
0.68700 |
0.20600 |
| 31.224 |
0.30000 |
0.60000 |
0.66500 |
0.28100 |
| 36.197 |
0.40000 |
0.20000 |
0.77200 |
0.11500 |
| 34.544 |
0.40000 |
0.40000 |
0.72600 |
0.19100 |
| 38.490 |
0.50000 |
0.10000 |
0.82600 |
0.06100 |
| 37.050 |
0.50000 |
0.30000 |
0.77100 |
0.14700 |
| 40.023 |
0.60000 |
0.10000 |
0.84400 |
0.05700 |
| 41.290 |
0.70000 |
0.20000 |
0.84500 |
0.10300 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| D'Avila S.G.; Cotrim M.L.: Prediction of Isothermal Vapor Liquid Equilibrium Data of Non Ideal Ternary Mixtures from Binary Data System: Acetone-Ethanol-Water. Rev.Bras.Tecnol. 4 (1973) 191-197 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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