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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
4792 Sodium nitrate 7631-99-4 NNaO3 Overview Details
Search for mixtures containing this mixture as subsystem
Search data for binary subsystems

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
Activity Coefficients at Infinite Dilution (Binary Solvents) ACM 2 7 303-333 Kn.a.
11 174 4792
2
Liquid-Liquid Equilibria (Miscibility Gaps) LLE 58 637 256-408 K101-102 kPa
4 11 39 174
1
4 39 174
16
11 39 174
34
39 174 4792
7
(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 7 144 293-374 K4-329 kPa
4 174 4792
2
11 174 4792
5
Densities and Volumes of Mixtures, Excess Volumes VE 12 411 283-353 Kn.a.
4 39 174
2
11 39 174
9
11 174 4792
1
Salt Solubilities ESLE 10 74 288-323 Kn.a.
4 174 4792
2
11 174 4792
6
39 174 4792
2
Mixture Viscosities VIS 8 80 288-343 Kn.a.
4 11 39
1
4 11 174
5
11 174 4792
2
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 5 49 308-473 K29-2471 kPa
4 174 4792
2
11 39 174
3
Mixture Flash Points MFLP 4 87 289-317 Kn.a.
11 39 174
4
Further Thermodynamic Properties X 2 21 298 K (const.)n.a.
4 11 39
1
4 11 39 174 4792
1
Total 148 2290
4 11 39
6
4 11 39 174
1
4 11 39 174 4792
1
4 11 174
12
4 39 174
24
4 174 4792
6
11 39 174
73
11 174 4792
16
39 174 4792
9

Dortmund Data Bank Version: February 2024
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