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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
3347 D-(+)-Saccharose 57-50-1 C12H22O11 Overview Details
Search for mixtures containing this mixture as subsystem
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Mixture Data

Databank Sets Points Temperature
Range
Pressure
Range
Vapor-Liquid Equilibria VLE 21 491 303-473 K12-2471 kPa
4 11 39
2
4 11 174
3
4 39 174
1
11 39 174
14
11 174 3347
1
Heats of Mixing HE 5 62 293-323 K101 kPa (const.)
4 11 174
1
4 39 174
4
Gas Solubilities GLE 1 1 310 K (const.)n.a.
4 174 3347
1
Liquid-Liquid Equilibria (Miscibility Gaps) LLE 53 593 256-395 K85-102 kPa
4 11 39 174
1
4 11 39 174 3347
1
4 39 174
16
11 39 174
34
39 174 3347
1
(A)zeotropic Data AZD 4 4 323 K (const.)97-102 kPa
4 11 39
1
4 11 174
1
11 39 174
2
Solid-Liquid Equilibria SLE 12 109 273-333 Kn.a.
4 11 174
1
11 174 3347
11
Densities and Volumes of Mixtures, Excess Volumes VE 18 372 283-353 Kn.a.
4 39 174
2
11 39 174
9
11 174 3347
7
Mixture Viscosities VIS 13 172 298-343 Kn.a.
4 11 39
1
4 11 174
5
11 174 3347
7
Mixture Surface Tensions MSFT 2 9 303-343 Kn.a.
4 11 39
1
4 11 174
1
Mixture Thermal Conductivities MTCN 10 239 293-353 Kn.a.
4 39 174
1
11 39 174
7
11 174 3347
2
Mixture P-v-T Data MPVT 9 179 281-473 K116-2471 kPa
11 39 174
3
11 174 3347
6
Mixture Flash Points MFLP 4 87 289-317 Kn.a.
11 39 174
4
Further Thermodynamic Properties X 23 190 273-313 Kn.a.
4 11 39
1
4 11 39 174 3347
1
4 174 3347
2
11 174 3347
19
Total 175 2508
4 11 39
6
4 11 39 174
1
4 11 39 174 3347
2
4 11 174
12
4 39 174
24
4 174 3347
3
11 39 174
73
11 174 3347
53
39 174 3347
1

Dortmund Data Bank Version: February 2024
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