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Thermophysical Data for Process Design
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DDB#
Name
CAS-RN
Formula
8
1,2-Ethanediol
107-21-1
C
2
H
6
O
2
Overview
Details
41
n-Butane
106-97-8
C
4
H
1
0
Overview
Details
174
Water
7732-18-5
H
2
O
Overview
Details
1051
Methane
74-82-8
CH
4
Overview
Details
1054
Ethane
74-84-0
C
2
H
6
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
65
629
117-411 K
117-100000 kPa
8
174
1051
16
8
174
1051
1054
2
8
174
1054
12
8
1051
1054
2
41
174
1051
7
41
174
1051
1054
8
41
1051
1054
2
174
1051
1054
16
Gas Solubilities
GLE
5
12
263-283 K
15000-30000 kPa
8
174
1051
5
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
1
4
344 K (const.)
2500-5000 kPa
41
174
1051
1
Solid-Liquid Equilibria
SLE
1
1
112 K (const.)
n.a.
41
1051
1054
1
Critical Data of Mixtures
CRI
2
10
319-380 K
5481-11721 kPa
41
1051
1054
2
Mixture Viscosities
VIS
4
42
265-468 K
101-13789 kPa
8
174
1051
3
41
1051
1054
1
Mixture Surface Tensions
MSFT
19
231
232-300 K
183-13789 kPa
8
174
1051
10
8
174
1054
9
Mixture P-v-T Data
MPVT
3
24
117-300 K
117-13789 kPa
8
174
1051
2
41
1051
1054
1
Gas Hydrate Data
GHD
142
982
233-314 K
240-172800 kPa
8
174
1051
35
8
174
1051
1054
3
8
174
1054
18
41
174
1051
29
41
174
1051
1054
3
41
174
1054
7
174
1051
1054
47
Further Thermodynamic Properties
X
37
622
201-422 K
200-54572 kPa
8
41
174
1051
1054
1
8
174
1051
7
8
174
1054
2
41
174
1051
3
41
174
1051
1054
7
41
1051
1054
1
174
1051
1054
16
Total
279
2557
8
41
174
1051
1054
1
8
174
1051
78
8
174
1051
1054
5
8
174
1054
41
8
1051
1054
2
41
174
1051
40
41
174
1051
1054
18
41
174
1054
7
41
1051
1054
8
174
1051
1054
79
Dortmund Data Bank Version: February 2024
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