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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
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
1065
Hydrogen sulfide
7783-06-4
H
2
S
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
92
865
179-344 K
480-19020 kPa
110
1050
1051
5
110
1050
1051
1056
1
110
1050
1051
1065
1
110
1050
1056
27
110
1050
1056
1065
3
1050
1051
1056
29
1050
1051
1065
25
1051
1056
1065
1
Heats of Mixing
HE
9
39
293-313 K
507-1529 kPa
1050
1051
1065
9
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
2
4
190-211 K
3682-7129 kPa
1050
1051
1065
2
(A)zeotropic Data
AZD
1
1
311 K (const.)
n.a.
1050
1051
1065
1
Solid-Liquid Equilibria
SLE
13
140
83-215 K
155-5570 kPa
110
1050
1051
1
1050
1051
1056
10
1050
1051
1065
2
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
1
2
270 K (const.)
9626-11146 kPa
1050
1051
1056
1
Mixture Viscosities
VIS
14
77
297-473 K
101-20884 kPa
1050
1051
1056
4
1050
1051
1065
10
Mixture Thermal Conductivities
MTCN
4
37
297-394 K
6986-21409 kPa
1050
1051
1065
4
Mixture P-v-T Data
MPVT
41
847
190-416 K
1-61697 kPa
1050
1051
1056
6
1050
1051
1056
1065
3
1050
1051
1065
21
1050
1056
1065
11
Further Thermodynamic Properties
X
61
1111
125-473 K
172-34336 kPa
110
1050
1051
1
110
1050
1051
1056
1065
1
110
1050
1056
4
110
1056
1065
1
1050
1051
1056
13
1050
1051
1065
33
1050
1056
1065
3
1051
1056
1065
5
Total
254
3394
110
1050
1051
7
110
1050
1051
1056
1
110
1050
1051
1056
1065
1
110
1050
1051
1065
1
110
1050
1056
31
110
1050
1056
1065
3
110
1056
1065
1
1050
1051
1056
79
1050
1051
1056
1065
3
1050
1051
1065
107
1050
1056
1065
14
1051
1056
1065
6
Dortmund Data Bank Version: February 2024
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