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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
546 Monoethanolamine 141-43-5 C2H7NO Overview Details
913 Ethanethiol 75-08-1 C2H6S Overview Details
1050 Carbon dioxide 124-38-9 CO2 Overview Details
1051 Methane 74-82-8 CH4 Overview Details
Search for mixtures containing this mixture as subsystem
Search data for binary subsystems

Mixture Data

Databank Sets Points Temperature
Range		 Pressure
Range
Vapor-Liquid Equilibria VLE 57 390 278-473 K4-103421 kPa
174 546 913 1051
2
174 546 1050
7
174 546 1051
3
174 913 1051
4
174 1050 1051
41
Gas Solubilities GLE 303 2370 273-423 K0-19954 kPa
174 546 913
1
174 546 1050
291
174 546 1051
11
Activity Coefficients at Infinite Dilution (Binary Solvents) ACM 1 6 298-348 Kn.a.
174 546 913
1
Liquid-Liquid Equilibria (Miscibility Gaps) LLE 2 22 288-364 K840-8268 kPa
174 913 1051
1
174 1050 1051
1
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 5 155 298-333 K800 kPa (const.)
174 546 1050
5
Critical Data of Mixtures CRI 1 7 288-304 K7615-8268 kPa
174 1050 1051
1
Mixture Viscosities VIS 118 1183 293-423 K100-400 kPa
174 546 1050
118
Mixture Surface Tensions MSFT 71 550 288-423 K97-33791 kPa
174 546 1050
34
174 1050 1051
37
Gas Hydrate Data GHD 78 685 189-294 K1100-40000 kPa
174 546 1051
2
174 1050 1051
76
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 144 2119 243-648 K1-27710 kPa
174 546 913 1050 1051
2
174 546 1050
121
174 546 1051
1
174 913 1051
1
174 1050 1051
19
Total 794 7578
174 546 913
2
174 546 913 1050 1051
2
174 546 913 1051
2
174 546 1050
590
174 546 1051
17
174 913 1051
6
174 1050 1051
175

Dortmund Data Bank Version: February 2024
What are "Sets" and "Points" in the Dortmund Data Bank? © Dortmund Data Bank  by  DDBST GmbH
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