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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
237 Propane 74-98-6 C3H8 Overview Details
1050 Carbon dioxide 124-38-9 CO2 Overview Details
1051 Methane 74-82-8 CH4 Overview Details
2187 Methyldiethanolamine (MDEA) 105-59-9 C5H13NO2 Overview Details
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Mixture Data

Databank Sets Points Temperature
Range		 Pressure
Range
Vapor-Liquid Equilibria VLE 298 3011 183-578 K2-103421 kPa
110 174 237
36
110 174 237 1050
4
110 174 1050
80
110 174 1050 1051
14
110 174 1051
50
110 174 2187
5
110 237 1050
8
110 237 1051
3
110 1050 1051
5
174 237 1050
2
174 237 1050 2187
5
174 237 1051
3
174 237 2187
7
174 1050 1051
41
174 1050 1051 2187
7
174 1050 2187
22
174 1051 2187
3
237 1050 1051
3
Heats of Mixing HE 21 176 300-400 K1380-6900 kPa
174 1050 1051 2187
21
Gas Solubilities GLE 397 2899 273-473 K0-20000 kPa
110 174 237
2
110 174 1050
47
110 174 1050 2187
3
110 174 1051
4
110 1050 2187
1
174 237 2187
5
174 1050 2187
323
174 1051 2187
12
Liquid-Liquid Equilibria (Miscibility Gaps) LLE 46 301 213-371 K45-20120 kPa
110 174 237
17
110 174 237 1050
4
110 174 237 1051
1
110 174 1050
5
110 237 1050
1
174 237 1050
5
174 237 1050 2187
3
174 237 2187
9
174 1050 1051
1
Heat Capacities of Mixtures, Excess Heat Capacities CPE 4 39 298 K (const.)n.a.
174 1050 2187
4
Solid-Liquid Equilibria SLE 2 16 150-211 K457-2365 kPa
110 1050 1051
1
237 1050 1051
1
Densities and Volumes of Mixtures, Excess Volumes VE 30 231 283-423 K101-808 kPa
110 174 2187
14
174 1050 2187
16
Critical Data of Mixtures CRI 2 20 288-328 K7615-10507 kPa
110 174 1050
1
174 1050 1051
1
Mixture Viscosities VIS 56 589 204-421 K100-30390 kPa
110 174 2187
28
174 1050 2187
25
237 1050 1051
3
Mixture Surface Tensions MSFT 54 775 288-423 K97-33791 kPa
110 174 1050
1
110 174 2187
7
174 1050 1051
37
174 1050 2187
8
174 1051 2187
1
Mixture P-v-T Data MPVT 40 869 273-423 K5-48442 kPa
110 174 237 1050 1051 2187
1
110 174 237 1051 2187
1
110 174 2187
3
110 237 1050
13
174 1050 2187
18
237 1050 1051
4
Gas Hydrate Data GHD 243 2127 189-353 K90-1,5E6 kPa
110 174 237
8
110 174 237 1050 1051
2
110 174 237 1051
8
110 174 1050
19
110 174 1050 1051
6
110 174 1051
30
174 237 1050
12
174 237 1050 1051
3
174 237 1051
73
174 1050 1051
76
174 1051 2187
6
Diffusion Coefficients DIF 6 48 288-323 Kn.a.
174 1050 2187
6
Further Thermodynamic Properties X 234 10758 191-648 K2-55261 kPa
110 174 237 1051
2
110 174 237 1051 2187
5
110 174 1050
1
110 174 1050 1051
2
110 174 1050 2187
2
110 174 1051
1
110 174 2187
3
110 1050 1051
1
174 237 1051
1
174 237 2187
1
174 1050 1051
19
174 1050 1051 2187
7
174 1050 2187
187
174 1051 2187
2
Total 1433 21859
110 174 237
63
110 174 237 1050
8
110 174 237 1050 1051
2
110 174 237 1050 1051 2187
1
110 174 237 1051
11
110 174 237 1051 2187
6
110 174 1050
154
110 174 1050 1051
22
110 174 1050 2187
5
110 174 1051
85
110 174 2187
60
110 237 1050
22
110 237 1051
3
110 1050 1051
7
110 1050 2187
1
174 237 1050
19
174 237 1050 1051
3
174 237 1050 2187
8
174 237 1051
77
174 237 2187
22
174 1050 1051
175
174 1050 1051 2187
35
174 1050 2187
609
174 1051 2187
24
237 1050 1051
11

Dortmund Data Bank Version: February 2024
What are "Sets" and "Points" in the Dortmund Data Bank? © Dortmund Data Bank  by  DDBST GmbH
Online DDB search information page Overall Statistics on Systems, Sets, and Points
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