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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
8 1,2-Ethanediol 107-21-1 C2H6O2 Overview Details
95 2-Propanol 67-63-0 C3H8O Overview Details
110 Methanol 67-56-1 CH4O 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 47 1237 308-523 K12-8198 kPa
4 8 110
1
4 8 174
1
4 95 110
4
4 95 110 174
1
4 95 174
15
4 110 174
17
8 95 174
2
95 110 174
6
Activity Coefficients at Infinite Dilution (Binary Solvents) ACM 2 45 298 K (const.)n.a.
95 110 174
2
(A)zeotropic Data AZD 6 6 323 K (const.)75-101 kPa
4 8 174
1
4 110 174
5
Solid-Liquid Equilibria SLE 2 56 218-270 Kn.a.
8 110 174
2
Densities and Volumes of Mixtures, Excess Volumes VE 37 571 283-308 K1010 kPa (const.)
4 8 174
2
4 95 110
1
4 95 174
24
4 110 174
5
8 95 174
3
95 110 174
2
Mixture Viscosities VIS 22 318 233-323 Kn.a.
4 8 110
1
4 110 174
4
8 110 174
10
95 110 174
7
Mixture Speeds of Sound MSOS 4 44 298-308 Kn.a.
8 95 174
3
8 110 174
1
Mixture Thermal Conductivities MTCN 6 34 313 K (const.)n.a.
4 8 95 110
2
4 8 95 110 174
1
8 95 110
1
8 95 174
1
95 110 174
1
Mixture P-v-T Data MPVT 1 5 308-348 K31-141 kPa
4 95 174
1
Mixture Flash Points MFLP 1 89 283-346 Kn.a.
95 110 174
1
Further Thermodynamic Properties X 8 97 271-323 K97-102 kPa
8 110 174
6
95 110 174
2
Total 136 2502
4 8 95 110
2
4 8 95 110 174
1
4 8 110
2
4 8 174
4
4 95 110
5
4 95 110 174
1
4 95 174
40
4 110 174
31
8 95 110
1
8 95 174
9
8 110 174
19
95 110 174
21

Dortmund Data Bank Version: February 2024
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