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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
4966 Potassium sulfate 7778-80-5 K2O4S Overview Details
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Mixture Data

Databank Sets Points Temperature
Range
Pressure
Range
Vapor-Liquid Equilibria VLE 20 462 303-473 K12-2471 kPa
4 11 39
2
4 11 174
3
4 39 174
1
11 39 174
14
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 51 549 256-395 K101-102 kPa
4 11 39 174
1
4 39 174
16
11 39 174
34
(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 1 10 277-288 Kn.a.
4 11 174
1
Vapor-Liquid Equilibria of Electrolyte Systems ELE 1 3 356-358 K101 kPa (const.)
11 174 4966
1
Densities and Volumes of Mixtures, Excess Volumes VE 21 513 283-353 Kn.a.
4 39 174
2
4 174 4966
3
11 39 174
9
11 174 4966
7
Salt Solubilities ESLE 30 223 277-373 Kn.a.
4 174 4966
11
11 174 4966
19
Mixture Viscosities VIS 7 78 293-343 Kn.a.
4 11 39
1
4 11 174
5
4 174 4966
1
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 3 35 373-473 K116-2471 kPa
11 39 174
3
Mixture Flash Points MFLP 4 87 289-317 Kn.a.
11 39 174
4
Further Thermodynamic Properties X 7 53 283-303 Kn.a.
4 11 39
1
4 11 39 174 4966
1
4 174 4966
4
11 174 4966
1
Total 164 2321
4 11 39
6
4 11 39 174
1
4 11 39 174 4966
1
4 11 174
12
4 39 174
24
4 174 4966
19
11 39 174
73
11 174 4966
28

Dortmund Data Bank Version: February 2024
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