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Thermophysical Data for Process Design
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DDB#
Name
CAS-RN
Formula
142
1-Propanethiol
107-03-9
C
3
H
8
S
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
1065
Hydrogen sulfide
7783-06-4
H
2
S
Overview
Details
1150
Dimethyl sulfide
75-18-3
C
2
H
6
S
Overview
Details
1934
n-Butylmercaptan
109-79-5
C
4
H
1
0
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
154
1083
190-606 K
6-103421 kPa
142
174
1051
3
142
1051
1934
6
174
1050
1051
41
174
1050
1051
1065
23
174
1050
1051
2187
7
174
1050
1065
10
174
1050
1065
2187
1
174
1050
2187
22
174
1051
1065
3
174
1051
1065
2187
2
174
1051
1150
3
174
1051
2187
3
174
1065
2187
5
1050
1051
1065
25
Heats of Mixing
HE
30
215
293-400 K
507-6900 kPa
174
1050
1051
2187
21
1050
1051
1065
9
Gas Solubilities
GLE
402
3036
283-473 K
0-1,8302E7 kPa
142
174
2187
3
174
1050
2187
323
174
1051
2187
12
174
1065
2187
58
174
1150
2187
3
174
1934
2187
3
Activity Coefficients at Infinite Dilution (Binary Solvents)
ACM
9
51
293-353 K
n.a.
142
174
2187
3
174
1150
2187
3
174
1934
2187
3
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
10
66
190-368 K
920-15400 kPa
142
174
1051
1
174
1050
1051
1
174
1050
1051
1065
1
174
1050
1065
4
174
1051
1934
1
1050
1051
1065
2
Heat Capacities of Mixtures, Excess Heat Capacities
CPE
4
39
298 K (const.)
n.a.
174
1050
2187
4
(A)zeotropic Data
AZD
1
1
311 K (const.)
n.a.
1050
1051
1065
1
Solid-Liquid Equilibria
SLE
2
12
183-210 K
604-2224 kPa
1050
1051
1065
2
Densities and Volumes of Mixtures, Excess Volumes
VE
16
108
298-423 K
101-808 kPa
174
1050
2187
16
Critical Data of Mixtures
CRI
1
7
288-304 K
7615-8268 kPa
174
1050
1051
1
Mixture Viscosities
VIS
44
376
293-394 K
6-20884 kPa
174
1050
1065
2187
3
174
1050
2187
25
174
1065
2187
6
1050
1051
1065
10
Mixture Surface Tensions
MSFT
58
653
288-423 K
97-68947 kPa
174
1050
1051
37
174
1050
1065
1
174
1050
1065
2187
3
174
1050
2187
8
174
1051
1065
6
174
1051
2187
1
174
1065
2187
2
Mixture Thermal Conductivities
MTCN
4
37
297-394 K
6986-21409 kPa
1050
1051
1065
4
Mixture P-v-T Data
MPVT
46
1163
190-423 K
5-31584 kPa
174
1050
1051
1065
1
174
1050
1065
2187
2
174
1050
2187
18
174
1065
2187
4
1050
1051
1065
21
Gas Hydrate Data
GHD
115
922
189-300 K
316-40000 kPa
142
174
1051
1
174
1050
1051
76
174
1050
1051
1065
17
174
1050
1065
7
174
1051
1065
7
174
1051
1934
1
174
1051
2187
6
Diffusion Coefficients
DIF
8
71
288-323 K
n.a.
174
1050
2187
6
174
1065
2187
2
Further Thermodynamic Properties
X
344
12253
174-648 K
2-34336 kPa
142
174
1050
1051
1065
1150
1934
2187
1
142
174
1050
1051
1065
2187
1
142
174
1050
1051
2187
1
142
174
1051
1
142
174
1051
1065
2187
1
142
174
1051
2187
2
174
1050
1051
19
174
1050
1051
1065
4
174
1050
1051
1065
2187
9
174
1050
1051
2187
7
174
1050
1065
1
174
1050
1065
2187
21
174
1050
2187
187
174
1051
1065
1
174
1051
1065
2187
11
174
1051
1934
1
174
1051
2187
2
174
1065
2187
41
1050
1051
1065
33
Total
1248
20093
142
174
1050
1051
1065
1150
1934
2187
1
142
174
1050
1051
1065
2187
1
142
174
1050
1051
2187
1
142
174
1051
6
142
174
1051
1065
2187
1
142
174
1051
2187
2
142
174
2187
6
142
1051
1934
6
174
1050
1051
175
174
1050
1051
1065
46
174
1050
1051
1065
2187
9
174
1050
1051
2187
35
174
1050
1065
23
174
1050
1065
2187
30
174
1050
2187
609
174
1051
1065
17
174
1051
1065
2187
13
174
1051
1150
3
174
1051
1934
3
174
1051
2187
24
174
1065
2187
118
174
1150
2187
6
174
1934
2187
6
1050
1051
1065
107
Dortmund Data Bank Version: February 2024
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