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Dortmund Data Bank
Thermophysical Data for Process Design
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DDB#
Name
CAS-RN
Formula
4
Acetone
67-64-1
C
3
H
6
O
Overview
Details
174
Water
7732-18-5
H
2
O
Overview
Details
1050
Carbon dioxide
124-38-9
CO
2
Overview
Details
1051
Methane
74-82-8
CH
4
Overview
Details
1056
Nitrogen
7727-37-9
N
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
107
1018
179-473 K
11-103421 kPa
4
174
1050
8
174
1050
1051
41
174
1050
1051
1056
1
174
1050
1056
22
174
1051
1056
6
1050
1051
1056
29
Gas Solubilities
GLE
32
378
213-395 K
63-9666 kPa
4
174
1050
29
4
174
1056
3
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
3
19
288-333 K
1836-8268 kPa
4
174
1050
2
174
1050
1051
1
Solid-Liquid Equilibria
SLE
10
124
83-215 K
155-5570 kPa
1050
1051
1056
10
Densities and Volumes of Mixtures, Excess Volumes
VE
16
271
323-573 K
19940-99930 kPa
1050
1051
1056
16
Critical Data of Mixtures
CRI
4
16
270-333 K
1741-11146 kPa
4
174
1050
2
174
1050
1051
1
1050
1051
1056
1
Mixture Viscosities
VIS
4
12
298-473 K
101 kPa (const.)
1050
1051
1056
4
Mixture Surface Tensions
MSFT
69
553
288-448 K
97-40000 kPa
174
1050
1051
37
174
1050
1056
17
174
1051
1056
15
Mixture P-v-T Data
MPVT
6
144
245-416 K
1275-61697 kPa
1050
1051
1056
6
Gas Hydrate Data
GHD
254
1866
189-300 K
100-55110 kPa
4
174
1050
21
4
174
1050
1051
4
4
174
1050
1051
1056
4
4
174
1051
26
4
174
1056
8
174
1050
1051
76
174
1050
1051
1056
31
174
1050
1056
64
174
1051
1056
20
Further Thermodynamic Properties
X
41
954
125-648 K
57-27710 kPa
4
174
1050
5
174
1050
1051
19
174
1050
1051
1056
1
174
1050
1056
3
1050
1051
1056
13
Total
546
5355
4
174
1050
67
4
174
1050
1051
4
4
174
1050
1051
1056
4
4
174
1051
26
4
174
1056
11
174
1050
1051
175
174
1050
1051
1056
33
174
1050
1056
106
174
1051
1056
41
1050
1051
1056
79
Dortmund Data Bank Version: February 2024
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