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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
110 Methanol 67-56-1 CH4O Overview Details
174 Water 7732-18-5 H2O Overview Details
546 Monoethanolamine 141-43-5 C2H7NO Overview Details
1050 Carbon dioxide 124-38-9 CO2 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 97 936 220-606 K4-35000 kPa
110 174 1050
80
174 546 1050
7
174 1050 1065
10
Gas Solubilities GLE 429 3455 273-423 K0-19954 kPa
110 174 1050
47
110 174 1065
1
110 546 1050
3
174 546 1050
291
174 546 1065
87
Liquid-Liquid Equilibria (Miscibility Gaps) LLE 9 25 223-333 K663-15400 kPa
110 174 1050
5
174 1050 1065
4
Heat Capacities of Mixtures, Excess Heat Capacities CPE 5 30 298 K (const.)n.a.
174 546 1050
5
Densities and Volumes of Mixtures, Excess Volumes VE 20 515 283-353 K800 kPa (const.)
110 174 546
15
174 546 1050
5
Critical Data of Mixtures CRI 1 13 318-328 K8927-10507 kPa
110 174 1050
1
Mixture Viscosities VIS 121 1210 293-423 K100-400 kPa
110 174 546
3
174 546 1050
118
Mixture Surface Tensions MSFT 40 355 288-350 K100-15600 kPa
110 174 546
4
110 174 1050
1
174 546 1050
34
174 1050 1065
1
Gas Hydrate Data GHD 38 270 233-300 K68-20705 kPa
110 174 1050
19
110 174 1065
12
174 1050 1065
7
Electrical Conductivities ECND 4 20 298 K (const.)100 kPa (const.)
174 546 1050
4
Diffusion Coefficients DIF 5 41 293-337 Kn.a.
174 546 1050
5
Further Thermodynamic Properties X 252 3520 283-413 K1-19950 kPa
110 174 546
1
110 174 546 1050
2
110 174 546 1050 1065
2
110 174 546 1065
2
110 174 1050
1
110 546 1050
3
174 546 1050
121
174 546 1050 1065
117
174 546 1065
2
174 1050 1065
1
Total 1021 10390
110 174 546
23
110 174 546 1050
2
110 174 546 1050 1065
2
110 174 546 1065
2
110 174 1050
154
110 174 1065
13
110 546 1050
6
174 546 1050
590
174 546 1050 1065
117
174 546 1065
89
174 1050 1065
23

Dortmund Data Bank Version: February 2024
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