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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
174
Water
7732-18-5
H
2
O
Overview
Details
443
Triethylene glycol
112-27-6
C
6
H
1
4
O
4
Overview
Details
1051
Methane
74-82-8
CH
4
Overview
Details
1065
Hydrogen sulfide
7783-06-4
H
2
S
Overview
Details
1363
Carbonyl sulfide
463-58-1
COS
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
50
376
250-353 K
471-46920 kPa
8
174
1051
16
8
174
1051
1363
1
8
174
1065
1
8
174
1065
1363
1
8
174
1363
3
8
1051
1065
2
174
443
1051
18
174
443
1051
1065
1
174
443
1065
1
174
443
1065
1363
1
174
443
1363
1
174
1051
1065
3
443
1065
1363
1
Gas Solubilities
GLE
33
220
263-363 K
11-30000 kPa
8
174
1051
5
8
174
1065
16
8
174
1363
9
174
443
1065
3
Solid-Liquid Equilibria
SLE
1
20
222-263 K
n.a.
8
174
443
1
Mixture Viscosities
VIS
5
47
265-333 K
3447-13789 kPa
8
174
1051
3
174
443
1051
1
174
443
1051
1065
1
Mixture Surface Tensions
MSFT
17
236
233-411 K
103-68947 kPa
8
174
1051
10
174
443
1051
1
174
1051
1065
6
Mixture P-v-T Data
MPVT
4
17
272-333 K
3447-13789 kPa
8
174
1051
2
174
443
1051
1
174
443
1051
1065
1
Gas Hydrate Data
GHD
67
342
233-298 K
103-39870 kPa
8
174
1051
35
8
174
1051
1065
3
8
174
1065
10
174
443
1051
11
174
443
1065
1
174
1051
1065
7
Diffusion Coefficients
DIF
1
1
298 K (const.)
n.a.
8
174
1363
1
Further Thermodynamic Properties
X
17
359
231-363 K
200-20684 kPa
8
174
443
1051
1065
1363
1
8
174
1051
7
8
174
1051
1065
2
8
174
1065
1
174
443
1051
4
174
443
1051
1065
1
174
1051
1065
1
Total
195
1618
8
174
443
1
8
174
443
1051
1065
1363
1
8
174
1051
78
8
174
1051
1065
5
8
174
1051
1363
1
8
174
1065
28
8
174
1065
1363
1
8
174
1363
13
8
1051
1065
2
174
443
1051
36
174
443
1051
1065
4
174
443
1065
5
174
443
1065
1363
1
174
443
1363
1
174
1051
1065
17
443
1065
1363
1
Dortmund Data Bank Version: February 2024
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