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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
1065
Hydrogen sulfide
7783-06-4
H
2
S
Overview
Details
2187
Methyldiethanolamine (MDEA)
105-59-9
C
5
H
1
3
NO
2
Overview
Details
2189
2-Amino-2-methyl-1-propanol (AMP)
124-68-5
C
4
H
1
1
NO
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
11
102
298-373 K
3-1093 kPa
174
894
2187
4
174
894
2189
1
174
1065
2187
5
174
2187
2189
1
Gas Solubilities
GLE
174
1718
283-422 K
0-1,8302E7 kPa
174
894
1065
90
174
894
1065
2187
5
174
1065
2187
58
174
1065
2187
2189
12
174
1065
2189
9
Heat Capacities of Mixtures, Excess Heat Capacities
CPE
23
355
298-353 K
n.a.
174
894
2187
12
174
894
2189
11
Densities and Volumes of Mixtures, Excess Volumes
VE
91
801
283-373 K
101 kPa (const.)
174
894
2187
39
174
894
2187
2189
6
174
894
2189
26
174
2187
2189
20
Mixture Viscosities
VIS
84
720
283-393 K
6-100000 kPa
174
894
1065
2
174
894
2187
26
174
894
2187
2189
4
174
894
2189
39
174
1065
2187
6
174
2187
2189
7
Mixture Surface Tensions
MSFT
25
352
288-373 K
150-13550 kPa
174
894
1065
2
174
894
2187
14
174
894
2187
2189
1
174
894
2189
2
174
1065
2187
2
174
2187
2189
4
Mixture P-v-T Data
MPVT
17
285
293-393 K
6-140000 kPa
174
894
1065
1
174
894
2187
12
174
1065
2187
4
Diffusion Coefficients
DIF
4
47
298-318 K
n.a.
174
894
1065
2187
1
174
894
2187
1
174
1065
2187
2
Further Thermodynamic Properties
X
92
2107
278-400 K
23-6895 kPa
174
894
1065
39
174
894
1065
2187
2189
9
174
894
2187
1
174
894
2187
2189
1
174
1065
2187
41
174
2187
2189
1
Total
521
6487
174
894
1065
134
174
894
1065
2187
6
174
894
1065
2187
2189
9
174
894
2187
109
174
894
2187
2189
12
174
894
2189
79
174
1065
2187
118
174
1065
2187
2189
12
174
1065
2189
9
174
2187
2189
33
Dortmund Data Bank Version: February 2024
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