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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
4 Acetone 67-64-1 C3H6O Overview Details
11 Ethanol 64-17-5 C2H6O Overview Details
39 1-Butanol 71-36-3 C4H10O Overview Details
174 Water 7732-18-5 H2O Overview Details
379 2-Ethyl-1-hexanol 104-76-7 C8H18O Overview Details
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Mixture Data

Databank Sets Points Temperature
Range
Pressure
Range
Vapor-Liquid Equilibria VLE 23 521 303-473 K12-2471 kPa
4 11 39
2
4 11 174
3
4 39 174
1
11 39 174
14
11 39 379
1
11 174 379
1
39 174 379
1
Heats of Mixing HE 5 62 293-323 K101 kPa (const.)
4 11 174
1
4 39 174
4
Liquid-Liquid Equilibria (Miscibility Gaps) LLE 77 765 256-473 K100-200000 kPa
4 11 39 174
1
4 11 39 174 379
1
4 39 174
16
4 174 379
5
11 39 174
34
11 174 379
12
39 174 379
8
(A)zeotropic Data AZD 5 5 323 K (const.)8-102 kPa
4 11 39
1
4 11 174
1
11 39 174
2
39 174 379
1
Solid-Liquid Equilibria SLE 1 10 277-288 Kn.a.
4 11 174
1
Densities and Volumes of Mixtures, Excess Volumes VE 11 323 283-353 Kn.a.
4 39 174
2
11 39 174
9
Mixture Viscosities VIS 6 72 298-343 Kn.a.
4 11 39
1
4 11 174
5
Mixture Surface Tensions MSFT 2 9 303-343 Kn.a.
4 11 39
1
4 11 174
1
Mixture Thermal Conductivities MTCN 8 233 293-353 Kn.a.
4 39 174
1
11 39 174
7
Mixture P-v-T Data MPVT 12 140 373-473 K60-2471 kPa
11 39 174
3
11 39 379
3
11 174 379
3
39 174 379
3
Mixture Flash Points MFLP 4 87 289-317 Kn.a.
11 39 174
4
Further Thermodynamic Properties X 1 20 n.a.n.a.
4 11 39
1
Total 155 2247
4 11 39
6
4 11 39 174
1
4 11 39 174 379
1
4 11 174
12
4 39 174
24
4 174 379
5
11 39 174
73
11 39 379
4
11 174 379
16
39 174 379
13

Dortmund Data Bank Version: February 2024
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