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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
H
2
O
Overview
Details
894
2,2'-Diethanolamine (DEA)
111-42-2
C
4
H
1
1
NO
2
Overview
Details
1050
Carbon dioxide
124-38-9
CO
2
Overview
Details
1051
Methane
74-82-8
CH
4
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
46
270
278-473 K
11-103421 kPa
174
894
1050
1051
3
174
894
1051
2
174
1050
1051
41
Heats of Mixing
HE
13
95
300-400 K
1380-3450 kPa
174
894
1050
1051
13
Gas Solubilities
GLE
203
1348
273-478 K
0-641691 kPa
174
894
1050
186
174
894
1050
1051
2
174
894
1051
15
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
1
7
288-304 K
7615-8268 kPa
174
1050
1051
1
Heat Capacities of Mixtures, Excess Heat Capacities
CPE
4
39
298 K (const.)
n.a.
174
894
1050
4
Densities and Volumes of Mixtures, Excess Volumes
VE
16
120
298-423 K
101-808 kPa
174
894
1050
16
Critical Data of Mixtures
CRI
1
7
288-304 K
7615-8268 kPa
174
1050
1051
1
Mixture Viscosities
VIS
7
83
293-353 K
n.a.
174
894
1050
7
Mixture Surface Tensions
MSFT
60
545
288-423 K
97-33791 kPa
174
894
1050
23
174
1050
1051
37
Mixture P-v-T Data
MPVT
13
579
293-423 K
100-13808 kPa
174
894
1050
13
Gas Hydrate Data
GHD
80
726
189-294 K
1100-40000 kPa
174
894
1051
4
174
1050
1051
76
Diffusion Coefficients
DIF
8
146
293-343 K
n.a.
174
894
1050
8
Further Thermodynamic Properties
X
120
2286
243-648 K
87-27710 kPa
174
894
1050
95
174
894
1050
1051
4
174
894
1051
2
174
1050
1051
19
Total
572
6251
174
894
1050
352
174
894
1050
1051
22
174
894
1051
23
174
1050
1051
175
Dortmund Data Bank Version: February 2024
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