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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
50 Cyclohexane 110-82-7 C6H12 Overview Details
174 Water 7732-18-5 H2O Overview Details
1050 Carbon dioxide 124-38-9 CO2 Overview Details
1065 Hydrogen sulfide 7783-06-4 H2S 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 38 352 289-606 K6-35000 kPa
174 1050 1065
10
174 1050 1065 2187
1
174 1050 2187
22
174 1065 2187
5
Gas Solubilities GLE 381 2898 283-473 K0-1,8302E7 kPa
174 1050 2187
323
174 1065 2187
58
Liquid-Liquid Equilibria (Miscibility Gaps) LLE 12 52 295-353 K416-15400 kPa
50 174 2187
8
174 1050 1065
4
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 34 311 293-382 K6-1093 kPa
174 1050 1065 2187
3
174 1050 2187
25
174 1065 2187
6
Mixture Surface Tensions MSFT 14 203 298-350 K110-15600 kPa
174 1050 1065
1
174 1050 1065 2187
3
174 1050 2187
8
174 1065 2187
2
Mixture P-v-T Data MPVT 24 547 293-423 K5-13862 kPa
174 1050 1065 2187
2
174 1050 2187
18
174 1065 2187
4
Gas Hydrate Data GHD 14 67 263-298 K202-10400 kPa
50 174 1050
6
50 174 1065
1
174 1050 1065
7
Diffusion Coefficients DIF 8 71 288-323 Kn.a.
174 1050 2187
6
174 1065 2187
2
Further Thermodynamic Properties X 268 10922 278-422 K2-19950 kPa
50 174 1050
1
50 174 1050 1065 2187
9
50 174 1050 2187
5
50 174 1065 2187
3
174 1050 1065
1
174 1050 1065 2187
21
174 1050 2187
187
174 1065 2187
41
Total 813 15570
50 174 1050
7
50 174 1050 1065 2187
9
50 174 1050 2187
5
50 174 1065
1
50 174 1065 2187
3
50 174 2187
8
174 1050 1065
23
174 1050 1065 2187
30
174 1050 2187
609
174 1065 2187
118

Dortmund Data Bank Version: February 2024
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