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Dortmund Data Bank
Thermophysical Data for Process Design
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DDB#
Name
CAS-RN
Formula
110
Methanol
67-56-1
CH
4
O
Overview
Details
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
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
95
836
220-578 K
4-23260 kPa
110
174
894
15
110
174
1050
80
Gas Solubilities
GLE
256
1846
273-478 K
0-641691 kPa
110
174
894
1050
23
110
174
1050
47
174
894
1050
186
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
5
11
223-311 K
663-8100 kPa
110
174
1050
5
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
39
225
278-423 K
101-808 kPa
110
174
894
23
174
894
1050
16
Critical Data of Mixtures
CRI
1
13
318-328 K
8927-10507 kPa
110
174
1050
1
Mixture Viscosities
VIS
10
110
293-353 K
101 kPa (const.)
110
174
894
3
174
894
1050
7
Mixture Surface Tensions
MSFT
27
311
288-353 K
100-15510 kPa
110
174
894
3
110
174
1050
1
174
894
1050
23
Mixture P-v-T Data
MPVT
30
681
283-423 K
100-13808 kPa
110
174
894
17
174
894
1050
13
Gas Hydrate Data
GHD
19
159
233-284 K
379-20705 kPa
110
174
1050
19
Diffusion Coefficients
DIF
8
146
293-343 K
n.a.
174
894
1050
8
Further Thermodynamic Properties
X
99
2114
278-400 K
71-9930 kPa
110
174
894
1
110
174
894
1050
2
110
174
1050
1
174
894
1050
95
Total
593
6491
110
174
894
62
110
174
894
1050
25
110
174
1050
154
174
894
1050
352
Dortmund Data Bank Version: February 2024
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