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Dortmund Data Bank
Thermophysical Data for Process Design
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DDB#
Name
CAS-RN
Formula
25
Ethylbenzene
100-41-4
C
8
H
1
0
Overview
Details
31
Benzene
71-43-2
C
6
H
6
Overview
Details
161
Toluene
108-88-3
C
7
H
8
Overview
Details
174
Water
7732-18-5
H
2
O
Overview
Details
1051
Methane
74-82-8
CH
4
Overview
Details
2187
Methyldiethanolamine (MDEA)
105-59-9
C
5
H
1
3
NO
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
9
85
300-399 K
101-13777 kPa
25
31
161
3
25
31
174
1
25
161
174
1
31
161
174
1
174
1051
2187
3
Gas Solubilities
GLE
12
87
298-423 K
12-20000 kPa
174
1051
2187
12
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
32
237
270-553 K
335-20000 kPa
25
31
161
174
2187
3
25
31
174
1
25
161
174
1
25
174
2187
2
31
161
174
2
31
161
174
2187
1
31
174
2187
4
161
174
1051
1
161
174
1051
2187
1
161
174
2187
16
(A)zeotropic Data
AZD
5
5
n.a.
98-101 kPa
25
31
161
2
25
31
174
2
31
161
174
1
Solid-Liquid Equilibria
SLE
4
15
276-278 K
n.a.
25
31
161
4
Mixture Viscosities
VIS
9
79
293-473 K
34570-138080 kPa
25
31
161
4
161
174
1051
5
Mixture Surface Tensions
MSFT
1
7
293-353 K
100 kPa (const.)
174
1051
2187
1
Gas Hydrate Data
GHD
14
60
274-292 K
1280-20260 kPa
31
174
1051
6
161
174
1051
2
174
1051
2187
6
Further Thermodynamic Properties
X
13
162
292-403 K
6-10997 kPa
25
31
161
174
1051
2187
2
25
174
1051
2187
1
31
174
2187
2
161
174
1051
2187
1
161
174
2187
5
174
1051
2187
2
Total
99
737
25
31
161
13
25
31
161
174
1051
2187
2
25
31
161
174
2187
3
25
31
174
4
25
161
174
2
25
174
1051
2187
1
25
174
2187
2
31
161
174
4
31
161
174
2187
1
31
174
1051
6
31
174
2187
6
161
174
1051
8
161
174
1051
2187
2
161
174
2187
21
174
1051
2187
24
Dortmund Data Bank Version: February 2024
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