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 Dortmund Data Bank
Thermophysical Data for Process Design
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DDB# Name CAS-RN Formula
174 Water 7732-18-5 H2O Overview Details
894 2,2'-Diethanolamine (DEA) 111-42-2 C4H11NO2 Overview Details
1050 Carbon dioxide 124-38-9 CO2 Overview Details
1065 Hydrogen sulfide 7783-06-4 H2S Overview Details
2189 2-Amino-2-methyl-1-propanol (AMP) 124-68-5 C4H11NO 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 14 167 293-606 K4-35000 kPa
174 894 2189
1
174 1050 1065
10
174 1050 2189
3
Gas Solubilities GLE 467 3788 273-478 K0-641691 kPa
174 894 1050
186
174 894 1050 2189
32
174 894 1065
90
174 1050 2189
150
174 1065 2189
9
Liquid-Liquid Equilibria (Miscibility Gaps) LLE 4 14 303-333 K4300-15400 kPa
174 1050 1065
4
Heat Capacities of Mixtures, Excess Heat Capacities CPE 15 215 298-353 Kn.a.
174 894 1050
4
174 894 2189
11
Densities and Volumes of Mixtures, Excess Volumes VE 42 320 293-423 K101-808 kPa
174 894 1050
16
174 894 2189
26
Mixture Viscosities VIS 53 486 293-353 Kn.a.
174 894 1050
7
174 894 1050 1065
2
174 894 1050 2189
3
174 894 1065
2
174 894 2189
39
Mixture Surface Tensions MSFT 30 328 293-353 K100-15600 kPa
174 894 1050
23
174 894 1050 1065
2
174 894 1065
2
174 894 2189
2
174 1050 1065
1
Mixture P-v-T Data MPVT 16 600 293-423 K100-13825 kPa
174 894 1050
13
174 894 1050 1065
2
174 894 1065
1
Gas Hydrate Data GHD 7 24 263-288 K316-10310 kPa
174 1050 1065
7
Diffusion Coefficients DIF 8 146 293-343 Kn.a.
174 894 1050
8
Further Thermodynamic Properties X 203 3598 278-400 K2-19950 kPa
174 894 1050
95
174 894 1050 1065
12
174 894 1050 1065 2189
8
174 894 1065
39
174 1050 1065
1
174 1050 1065 2189
4
174 1050 2189
44
Total 859 9686
174 894 1050
352
174 894 1050 1065
18
174 894 1050 1065 2189
8
174 894 1050 2189
35
174 894 1065
134
174 894 2189
79
174 1050 1065
23
174 1050 1065 2189
4
174 1050 2189
197
174 1065 2189
9

Dortmund Data Bank Version: February 2024
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