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 Dortmund Data Bank
Thermophysical Data for Process Design
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Query
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DDB# Name CAS-RN Formula
3 Acetonitrile 75-05-8 C2H3N Overview Details
11 Ethanol 64-17-5 C2H6O Overview Details
21 Ethyl acetate 141-78-6 C4H8O2 Overview Details
84 Acetic acid 64-19-7 C2H4O2 Overview Details
174 Water 7732-18-5 H2O Overview Details
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Mixture Data

Databank Sets Points Temperature
Range		 Pressure
Range
Vapor-Liquid Equilibria VLE 27 1003 313-391 K19-137 kPa
3 11 174
2
11 21 84 174
4
11 21 174
19
21 84 174
2
Heats of Mixing HE 3 56 298-313 K100-101 kPa
11 21 84
1
11 21 84 174
2
Activity Coefficients at Infinite Dilution (Binary Solvents) ACM 1 29 298 K (const.)n.a.
3 11 174
1
Liquid-Liquid Equilibria (Miscibility Gaps) LLE 134 1565 273-351 K100-101 kPa
3 21 174
3
11 21 84 174
26
11 21 174
58
21 84 174
47
(A)zeotropic Data AZD 25 25 272-362 K3-193 kPa
3 11 174
5
11 21 174
19
11 84 174
1
Densities and Volumes of Mixtures, Excess Volumes VE 23 899 288-343 K101 kPa (const.)
11 21 174
19
11 84 174
2
21 84 174
2
Critical Data of Mixtures CRI 2 12 293-553 K101-7440 kPa
11 21 84 174
2
Mixture Viscosities VIS 5 243 298-318 K101 kPa (const.)
11 21 174
2
11 84 174
3
Mixture Surface Tensions MSFT 2 46 263-298 K101 kPa (const.)
3 11 174
1
3 21 174
1
Mixture Speeds of Sound MSOS 15 510 288-323 K101 kPa (const.)
11 21 174
15
Mixture Thermal Conductivities MTCN 3 18 293-333 Kn.a.
11 21 174
3
Diffusion Coefficients DIF 6 24 288-318 Kn.a.
11 84 174
6
Further Thermodynamic Properties X 11 248 295-343 K101 kPa (const.)
3 11 21 84 174
1
3 11 174
1
11 21 84 174
7
11 84 174
1
21 84 174
1
Total 257 4678
3 11 21 84 174
1
3 11 174
10
3 21 174
4
11 21 84
1
11 21 84 174
41
11 21 174
135
11 84 174
13
21 84 174
52

Dortmund Data Bank Version: February 2024
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