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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
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
1056 Nitrogen 7727-37-9 N2 Overview Details
1065 Hydrogen sulfide 7783-06-4 H2S 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 33 315 273-606 K101-35000 kPa
174 1050 1056
22
174 1050 1056 1065
1
174 1050 1065
10
Gas Solubilities GLE 276 2250 273-478 K0-641691 kPa
174 894 1050
186
174 894 1065
90
Liquid-Liquid Equilibria (Miscibility Gaps) LLE 5 19 292-334 K4300-15400 kPa
174 1050 1056 1065
1
174 1050 1065
4
Heat Capacities of Mixtures, Excess Heat Capacities CPE 4 39 298 K (const.)n.a.
174 894 1050
4
Densities and Volumes of Mixtures, Excess Volumes VE 16 120 298-423 K101-808 kPa
174 894 1050
16
Mixture Viscosities VIS 11 136 293-353 Kn.a.
174 894 1050
7
174 894 1050 1065
2
174 894 1065
2
Mixture Surface Tensions MSFT 45 397 293-448 K100-40000 kPa
174 894 1050
23
174 894 1050 1065
2
174 894 1065
2
174 1050 1056
17
174 1050 1065
1
Mixture P-v-T Data MPVT 27 676 292-423 K1-13996 kPa
174 894 1050
13
174 894 1050 1065
2
174 894 1065
1
1050 1056 1065
11
Gas Hydrate Data GHD 71 486 263-289 K100-55110 kPa
174 1050 1056
64
174 1050 1065
7
Diffusion Coefficients DIF 8 146 293-343 Kn.a.
174 894 1050
8
Further Thermodynamic Properties X 196 3503 278-400 K87-19950 kPa
174 894 1050
95
174 894 1050 1056
9
174 894 1050 1056 1065
22
174 894 1050 1065
12
174 894 1056 1065
10
174 894 1065
39
174 1050 1056
3
174 1050 1056 1065
2
174 1050 1065
1
1050 1056 1065
3
Total 692 8087
174 894 1050
352
174 894 1050 1056
9
174 894 1050 1056 1065
22
174 894 1050 1065
18
174 894 1056 1065
10
174 894 1065
134
174 1050 1056
106
174 1050 1056 1065
4
174 1050 1065
23
1050 1056 1065
14

Dortmund Data Bank Version: February 2024
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