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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
8 1,2-Ethanediol 107-21-1 C2H6O2 Overview Details
174 Water 7732-18-5 H2O Overview Details
1050 Carbon dioxide 124-38-9 CO2 Overview Details
1051 Methane 74-82-8 CH4 Overview Details
1054 Ethane 74-84-0 C2H6 Overview Details
1056 Nitrogen 7727-37-9 N2 Overview Details
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Mixture Data

Databank Sets Points Temperature
Range		 Pressure
Range
Vapor-Liquid Equilibria VLE 222 2321 96-473 K9-103421 kPa
8 174 1050
10
8 174 1050 1051
1
8 174 1051
16
8 174 1051 1054
2
8 174 1054
12
8 174 1056
5
8 1051 1054
2
174 1050 1051
41
174 1050 1051 1054
2
174 1050 1051 1056
1
174 1050 1054
6
174 1050 1056
22
174 1051 1054
16
174 1051 1056
6
1050 1051 1054
9
1050 1051 1056
29
1050 1054 1056
7
1051 1054 1056
35
Gas Solubilities GLE 27 83 250-333 K100-30000 kPa
8 174 1050
17
8 174 1051
5
8 174 1056
5
Liquid-Liquid Equilibria (Miscibility Gaps) LLE 15 59 109-304 K1309-8268 kPa
174 1050 1051
1
1051 1054 1056
14
(A)zeotropic Data AZD 1 1 230 K (const.)n.a.
1050 1051 1054
1
Solid-Liquid Equilibria SLE 18 271 83-215 K155-5570 kPa
1050 1051 1054
7
1050 1051 1056
10
1050 1054 1056
1
Densities and Volumes of Mixtures, Excess Volumes VE 16 271 323-573 K19940-99930 kPa
1050 1051 1056
16
Critical Data of Mixtures CRI 2 9 270-304 K7615-11146 kPa
174 1050 1051
1
1050 1051 1056
1
Mixture Viscosities VIS 15 255 122-473 K101-13789 kPa
8 174 1050 1051
1
8 174 1051
3
8 174 1056
5
1050 1051 1056
4
1051 1054 1056
2
Mixture Surface Tensions MSFT 98 896 227-448 K97-40000 kPa
8 174 1050 1051
1
8 174 1051
10
8 174 1054
9
8 174 1056
9
174 1050 1051
37
174 1050 1056
17
174 1051 1056
15
Mixture Dielectric Constants MDEC 1 4 91-115 K49-221 kPa
1051 1054 1056
1
Mixture P-v-T Data MPVT 40 673 91-416 K36-61697 kPa
8 174 1050 1051
1
8 174 1051
2
1050 1051 1054
7
1050 1051 1054 1056
10
1050 1051 1056
6
1051 1054 1056
14
Gas Hydrate Data GHD 344 2514 189-314 K100-172800 kPa
8 174 1050
18
8 174 1050 1051
3
8 174 1050 1051 1054 1056
1
8 174 1050 1051 1056
2
8 174 1050 1054
1
8 174 1050 1056
2
8 174 1051
35
8 174 1051 1054
3
8 174 1054
18
174 1050 1051
76
174 1050 1051 1054
9
174 1050 1051 1054 1056
2
174 1050 1051 1056
31
174 1050 1054
11
174 1050 1056
64
174 1051 1054
47
174 1051 1054 1056
1
174 1051 1056
20
Diffusion Coefficients DIF 2 13 298 K (const.)101 kPa (const.)
8 174 1050
2
Further Thermodynamic Properties X 85 1695 116-648 K110-54572 kPa
8 174 1050
1
8 174 1050 1051
2
8 174 1051
7
8 174 1054
2
8 174 1056
1
174 1050 1051
19
174 1050 1051 1056
1
174 1050 1054
4
174 1050 1056
3
174 1051 1054
16
1050 1051 1054
6
1050 1051 1056
13
1051 1054 1056
10
Total 886 9065
8 174 1050
48
8 174 1050 1051
9
8 174 1050 1051 1054 1056
1
8 174 1050 1051 1056
2
8 174 1050 1054
1
8 174 1050 1056
2
8 174 1051
78
8 174 1051 1054
5
8 174 1054
41
8 174 1056
25
8 1051 1054
2
174 1050 1051
175
174 1050 1051 1054
11
174 1050 1051 1054 1056
2
174 1050 1051 1056
33
174 1050 1054
21
174 1050 1056
106
174 1051 1054
79
174 1051 1054 1056
1
174 1051 1056
41
1050 1051 1054
30
1050 1051 1054 1056
10
1050 1051 1056
79
1050 1054 1056
8
1051 1054 1056
76

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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