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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
174 Water 7732-18-5 H2O Overview Details
1050 Carbon dioxide 124-38-9 CO2 Overview Details
1061 Dinitrogen monoxide 10024-97-2 N2O Overview Details
2187 Methyldiethanolamine (MDEA) 105-59-9 C5H13NO2 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 118 960 274-398 K7-30000 kPa
11 174 1050
83
174 1050 2187
22
174 1061 2187
13
Heats of Mixing HE 15 337 308-323 K7500-15000 kPa
11 174 1050
15
Gas Solubilities GLE 414 2848 206-473 K0-19854 kPa
11 174 1050
42
11 174 1061
4
11 1050 2187
1
11 1061 2187
1
174 1050 2187
323
174 1061 2187
43
Liquid-Liquid Equilibria (Miscibility Gaps) LLE 15 39 274-313 K3200-20570 kPa
11 174 1050
12
11 174 1061
1
174 1061 2187
2
Heat Capacities of Mixtures, Excess Heat Capacities CPE 4 39 298 K (const.)n.a.
174 1050 2187
4
Densities and Volumes of Mixtures, Excess Volumes VE 16 108 298-423 K101-808 kPa
174 1050 2187
16
Mixture Viscosities VIS 27 221 293-382 Kn.a.
174 1050 1061 2187
1
174 1050 2187
25
174 1061 2187
1
Mixture Surface Tensions MSFT 18 349 278-345 K100-17230 kPa
11 174 1050
10
174 1050 2187
8
Mixture Speeds of Sound MSOS 8 96 288-323 Kn.a.
11 174 2187
8
Mixture P-v-T Data MPVT 18 493 293-423 K5-13810 kPa
174 1050 2187
18
Gas Hydrate Data GHD 13 68 268-280 K950-3760 kPa
11 174 1050
11
174 1050 1061
2
Diffusion Coefficients DIF 29 231 288-368 Kn.a.
11 174 1050 1061 2187
1
174 1050 2187
6
174 1061 2187
22
Further Thermodynamic Properties X 199 9915 278-422 K2-13150 kPa
11 174 1050
6
174 1050 1061 2187
6
174 1050 2187
187
Total 894 15704
11 174 1050
179
11 174 1050 1061 2187
1
11 174 1061
5
11 174 2187
8
11 1050 2187
1
11 1061 2187
1
174 1050 1061
2
174 1050 1061 2187
7
174 1050 2187
609
174 1061 2187
81

Dortmund Data Bank Version: February 2024
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