Dortmund Data Bank
Vapor Pressure of Ethanol
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.
Component
| Formula |
Molar Mass |
CAS Registry Number |
Name |
| C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of Ethanol
Diagrams
Data Table
| T [K] |
P [kPa] |
State |
Reference |
| 273.15 |
1.5932 |
Vapor-Liquid |
6 |
| 277.24 |
2.1065 |
Vapor-Liquid |
1 |
| 277.24 |
2.112 |
Vapor-Liquid |
1 |
| 278.12 |
2.233 |
Vapor-Liquid |
1 |
| 278.12 |
2.2425 |
Vapor-Liquid |
1 |
| 278.15 |
2.2395 |
Vapor-Liquid |
4 |
| 281.45 |
2.760 |
Vapor-Liquid |
2 |
| 281.55 |
2.800 |
Vapor-Liquid |
2 |
| 282.15 |
2.920 |
Vapor-Liquid |
2 |
| 282.45 |
2.9464 |
Vapor-Liquid |
2 |
| 282.85 |
3.040 |
Vapor-Liquid |
2 |
| 283.14 |
3.108 |
Vapor-Liquid |
1 |
| 283.14 |
3.129 |
Vapor-Liquid |
1 |
| 283.15 |
3.140 |
Vapor-Liquid |
3 |
| 283.35 |
3.133 |
Vapor-Liquid |
2 |
| 283.75 |
3.2264 |
Vapor-Liquid |
2 |
| 284.15 |
3.2664 |
Vapor-Liquid |
2 |
| 284.75 |
3.413 |
Vapor-Liquid |
2 |
| 284.95 |
3.5064 |
Vapor-Liquid |
2 |
| 285.25 |
3.5464 |
Vapor-Liquid |
2 |
| 285.55 |
3.6264 |
Vapor-Liquid |
2 |
| 286.05 |
3.693 |
Vapor-Liquid |
2 |
| 286.35 |
3.813 |
Vapor-Liquid |
2 |
| 286.75 |
3.880 |
Vapor-Liquid |
2 |
| 287.05 |
3.986 |
Vapor-Liquid |
2 |
| 287.25 |
4.013 |
Vapor-Liquid |
2 |
| 287.95 |
4.200 |
Vapor-Liquid |
2 |
| 288.11 |
4.276 |
Vapor-Liquid |
1 |
| 288.11 |
4.302 |
Vapor-Liquid |
1 |
| 288.35 |
4.306 |
Vapor-Liquid |
2 |
| 289.05 |
4.493 |
Vapor-Liquid |
2 |
| 289.05 |
4.520 |
Vapor-Liquid |
2 |
| 289.45 |
4.586 |
Vapor-Liquid |
2 |
| 289.65 |
4.666 |
Vapor-Liquid |
2 |
| 289.85 |
4.786 |
Vapor-Liquid |
2 |
| 290.25 |
4.840 |
Vapor-Liquid |
2 |
| 290.35 |
4.853 |
Vapor-Liquid |
2 |
| 290.65 |
4.960 |
Vapor-Liquid |
2 |
| 291.05 |
5.080 |
Vapor-Liquid |
2 |
| 291.45 |
5.186 |
Vapor-Liquid |
2 |
| 291.75 |
5.333 |
Vapor-Liquid |
2 |
| 291.85 |
5.320 |
Vapor-Liquid |
2 |
| 292.25 |
5.466 |
Vapor-Liquid |
2 |
| 292.45 |
5.546 |
Vapor-Liquid |
2 |
| 292.65 |
5.613 |
Vapor-Liquid |
2 |
| 293.05 |
5.760 |
Vapor-Liquid |
2 |
| 293.15 |
5.786 |
Vapor-Liquid |
2 |
| 293.15 |
5.865 |
Vapor-Liquid |
4 |
| 293.20 |
5.860 |
Vapor-Liquid |
3 |
| 293.20 |
5.864 |
Vapor-Liquid |
1 |
| 293.20 |
5.882 |
Vapor-Liquid |
1 |
| 293.35 |
5.893 |
Vapor-Liquid |
2 |
| 293.65 |
5.960 |
Vapor-Liquid |
2 |
| 293.75 |
6.026 |
Vapor-Liquid |
2 |
| 294.25 |
6.173 |
Vapor-Liquid |
2 |
| 294.25 |
6.199 |
Vapor-Liquid |
2 |
| 294.65 |
6.319 |
Vapor-Liquid |
2 |
| 294.75 |
6.359 |
Vapor-Liquid |
2 |
| 294.95 |
6.426 |
Vapor-Liquid |
2 |
| 295.25 |
6.533 |
Vapor-Liquid |
2 |
| 295.45 |
6.599 |
Vapor-Liquid |
2 |
| 295.45 |
6.653 |
Vapor-Liquid |
2 |
| 295.55 |
6.533 |
Vapor-Liquid |
2 |
| 295.65 |
6.733 |
Vapor-Liquid |
2 |
| 295.85 |
6.773 |
Vapor-Liquid |
2 |
| 295.95 |
6.866 |
Vapor-Liquid |
2 |
| 296.05 |
6.879 |
Vapor-Liquid |
2 |
| 296.25 |
6.946 |
Vapor-Liquid |
2 |
| 296.35 |
7.026 |
Vapor-Liquid |
2 |
| 296.55 |
7.066 |
Vapor-Liquid |
2 |
| 296.65 |
7.146 |
Vapor-Liquid |
2 |
| 298.12 |
7.883 |
Vapor-Liquid |
1 |
| 298.12 |
7.889 |
Vapor-Liquid |
1 |
| 298.15 |
7.869 |
Vapor-Liquid |
6 |
| 303.16 |
10.454 |
Vapor-Liquid |
1 |
| 303.16 |
10.460 |
Vapor-Liquid |
1 |
| 303.20 |
10.479 |
Vapor-Liquid |
3 |
| 307.65 |
13.372 |
Vapor-Liquid |
2 |
| 308.14 |
13.736 |
Vapor-Liquid |
6 |
| 308.15 |
13.672 |
Vapor-Liquid |
3 |
| 308.15 |
13.703 |
Vapor-Liquid |
5 |
| 308.15 |
13.760 |
Vapor-Liquid |
4 |
| 308.18 |
13.777 |
Vapor-Liquid |
1 |
| 308.18 |
13.785 |
Vapor-Liquid |
1 |
| 313.15 |
17.877 |
Vapor-Liquid |
5 |
| 313.17 |
17.909 |
Vapor-Liquid |
1 |
| 313.17 |
17.916 |
Vapor-Liquid |
1 |
| 314.85 |
19.985 |
Vapor-Liquid |
2 |
| 315.55 |
20.225 |
Vapor-Liquid |
2 |
| 318.14 |
23.058 |
Vapor-Liquid |
6 |
| 318.15 |
23.033 |
Vapor-Liquid |
5 |
| 318.18 |
23.093 |
Vapor-Liquid |
1 |
| 318.18 |
23.119 |
Vapor-Liquid |
1 |
| 319.17 |
24.247 |
Vapor-Liquid |
1 |
| 319.17 |
24.257 |
Vapor-Liquid |
1 |
| 321.05 |
26.798 |
Vapor-Liquid |
2 |
| 323.15 |
29.456 |
Vapor-Liquid |
6 |
| 323.15 |
29.488 |
Vapor-Liquid |
5 |
| 323.15 |
29.491 |
Vapor-Liquid |
4 |
| 325.55 |
33.411 |
Vapor-Liquid |
2 |
| 328.14 |
37.302 |
Vapor-Liquid |
6 |
| 328.15 |
37.312 |
Vapor-Liquid |
5 |
| 329.55 |
39.757 |
Vapor-Liquid |
2 |
| 329.65 |
40.010 |
Vapor-Liquid |
2 |
| 333.15 |
46.839 |
Vapor-Liquid |
5 |
| 335.85 |
53.356 |
Vapor-Liquid |
2 |
| 338.15 |
58.358 |
Vapor-Liquid |
4 |
| 338.15 |
58.400 |
Vapor-Liquid |
6 |
| 338.15 |
58.443 |
Vapor-Liquid |
5 |
| 340.85 |
66.874 |
Vapor-Liquid |
2 |
| 341.15 |
67.154 |
Vapor-Liquid |
2 |
| 343.15 |
72.273 |
Vapor-Liquid |
5 |
| 345.15 |
80.180 |
Vapor-Liquid |
2 |
| 348.15 |
88.858 |
Vapor-Liquid |
5 |
| 348.55 |
93.432 |
Vapor-Liquid |
2 |
| 349.05 |
93.846 |
Vapor-Liquid |
2 |
| 350.75 |
99.698 |
Vapor-Liquid |
2 |
| 350.85 |
100.045 |
Vapor-Liquid |
2 |
| 351.15 |
101.325 |
Vapor-Liquid |
2 |
| 351.25 |
101.325 |
Vapor-Liquid |
2 |
| 351.70 |
102.220 |
Vapor-Liquid |
6 |
List of References
| Number |
Source |
| 1 |
Mishchenko K.P.; Subbotina V.V.: Dampfdruck von Ethanol bei Temperaturen von 4 bis 46°C. Zh.Prikl.Khim. 40 (1967) 1156-1159 |
| 2 |
Kahlbaum G.W.A.; von Wirkner C.G.: 1.Hälfte (Vol. 2a). Monograph (1897) 1-222 |
| 3 |
Chun K.W.; Davison R.R.: Thermodynamic Properties of Binary Mixtures of Triethylamine with Methyl and Ethyl Alcohol. J.Chem.Eng.Data 17 (1972) 307-310 |
| 4 |
Scatchard G.; Satkiewicz F.G.: XII. The System Ethanol-Cyclohexane from 5 to 65°. J.Am.Chem.Soc. 86 (1964) 130-133 |
| 5 |
Scatchard G.; Raymond C.L.: II. Chloroform-Ethanol Mixtures at 35, 45 and 55 °. J.Am.Chem.Soc. 60 (1938) 1278-1287 |
| 6 |
Kretschmer C.B.; Wiebe R.: Liquid-Vapor Equilibrium of Ethanol-Toluene Solutions. J.Am.Chem.Soc. 71 (1949) 1793-1797 |
Pure Component Data Overview
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