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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
11 Ethanol 64-17-5 C2H6O Overview Details
31 Benzene 71-43-2 C6H6 Overview Details
80 Butyl acetate 123-86-4 C6H12O2 Overview Details
174 Water 7732-18-5 H2O 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 20 700 308-413 K26-949 kPa
11 31 80
1
11 31 80 174
4
11 31 174
10
11 80 174
4
31 80 174
1
Activity Coefficients at Infinite Dilution (Binary Solvents) ACM 1 5 295 K (const.)n.a.
11 31 174
1
Liquid-Liquid Equilibria (Miscibility Gaps) LLE 112 624 272-361 K48-101 kPa
11 31 80 174
1
11 31 174
96
11 80 174
11
31 80 174
4
(A)zeotropic Data AZD 26 26 306-445 K29-1937 kPa
11 31 174
24
11 80 174
1
31 80 174
1
Solid-Liquid Equilibria SLE 8 66 267-277 Kn.a.
11 31 174
8
Densities and Volumes of Mixtures, Excess Volumes VE 2 82 293-298 Kn.a.
11 31 174
2
Mixture Surface Tensions MSFT 2 19 293-298 Kn.a.
11 31 174
2
Further Thermodynamic Properties X 5 33 263-303 Kn.a.
11 31 174
5
Total 176 1555
11 31 80
1
11 31 80 174
5
11 31 174
148
11 80 174
16
31 80 174
6

Dortmund Data Bank Version: February 2024
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