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Thermophysical Data for Process Design
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DDB#
Name
CAS-RN
Formula
174
Water
7732-18-5
H
2
O
Overview
Details
180
2-Propanethiol
75-33-2
C
3
H
8
S
Overview
Details
579
Methanethiol
74-93-1
CH
4
S
Overview
Details
1051
Methane
74-82-8
CH
4
Overview
Details
1065
Hydrogen sulfide
7783-06-4
H
2
S
Overview
Details
1150
Dimethyl sulfide
75-18-3
C
2
H
6
S
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
27
172
300-373 K
6-14796 kPa
174
579
1051
9
174
579
1051
2187
2
174
1051
1065
3
174
1051
1065
2187
2
174
1051
1150
3
174
1051
2187
3
174
1065
2187
5
Gas Solubilities
GLE
80
676
283-423 K
0-1,8302E7 kPa
174
180
2187
4
174
579
2187
3
174
1051
2187
12
174
1065
2187
58
174
1150
2187
3
Activity Coefficients at Infinite Dilution (Binary Solvents)
ACM
7
42
293-348 K
n.a.
174
180
2187
2
174
579
2187
2
174
1150
2187
3
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
1
39
304-364 K
1210-9184 kPa
174
579
1051
1
Mixture Viscosities
VIS
6
81
293-353 K
6-1093 kPa
174
1065
2187
6
Mixture Surface Tensions
MSFT
9
140
293-411 K
100-68947 kPa
174
1051
1065
6
174
1051
2187
1
174
1065
2187
2
Mixture P-v-T Data
MPVT
4
39
313-344 K
6-13862 kPa
174
1065
2187
4
Gas Hydrate Data
GHD
13
73
274-298 K
920-20260 kPa
174
1051
1065
7
174
1051
2187
6
Diffusion Coefficients
DIF
2
23
298-299 K
n.a.
174
1065
2187
2
Further Thermodynamic Properties
X
61
893
278-400 K
23-10997 kPa
174
180
579
1051
1065
1150
2187
2
174
180
579
1051
1150
2187
1
174
579
1051
1
174
579
1051
1065
2187
2
174
1051
1065
1
174
1051
1065
2187
11
174
1051
2187
2
174
1065
2187
41
Total
210
2178
174
180
579
1051
1065
1150
2187
2
174
180
579
1051
1150
2187
1
174
180
2187
6
174
579
1051
11
174
579
1051
1065
2187
2
174
579
1051
2187
2
174
579
2187
5
174
1051
1065
17
174
1051
1065
2187
13
174
1051
1150
3
174
1051
2187
24
174
1065
2187
118
174
1150
2187
6
Dortmund Data Bank Version: February 2024
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