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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
546
Monoethanolamine
141-43-5
C
2
H
7
NO
Overview
Details
1050
Carbon dioxide
124-38-9
CO
2
Overview
Details
1056
Nitrogen
7727-37-9
N
2
Overview
Details
17173
1-Butyl-3-methylimidazolium tetrafluoroborate
174501-65-6
C
8
H
1
5
BF
4
N
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
35
387
273-473 K
4-29420 kPa
174
546
1050
7
174
546
17173
2
174
1050
1056
22
174
1050
17173
1
546
1050
17173
3
Gas Solubilities
GLE
299
2381
273-423 K
0-19954 kPa
174
546
1050
291
174
546
1050
17173
1
174
1050
17173
5
546
1050
17173
2
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
2
10
278-297 K
3500-16000 kPa
174
1050
17173
2
Heat Capacities of Mixtures, Excess Heat Capacities
CPE
5
30
298 K (const.)
n.a.
174
546
1050
5
Densities and Volumes of Mixtures, Excess Volumes
VE
32
371
293-353 K
101-800 kPa
174
546
1050
5
174
546
17173
27
Mixture Viscosities
VIS
147
1423
293-423 K
100-400 kPa
174
546
1050
118
174
546
1050
1056
1
174
546
17173
28
Mixture Surface Tensions
MSFT
55
370
293-448 K
100-40000 kPa
174
546
1050
34
174
546
17173
4
174
1050
1056
17
Mixture P-v-T Data
MPVT
1
1
313 K (const.)
n.a.
174
546
1050
1056
1
Gas Hydrate Data
GHD
65
466
272-289 K
100-55110 kPa
174
1050
1056
64
174
1050
17173
1
Electrical Conductivities
ECND
4
20
298 K (const.)
100 kPa (const.)
174
546
1050
4
Diffusion Coefficients
DIF
5
41
293-337 K
n.a.
174
546
1050
5
Further Thermodynamic Properties
X
147
1877
293-393 K
1-8740 kPa
174
546
1050
121
174
546
1050
1056
12
174
546
1050
1056
17173
2
174
546
1056
1
174
1050
1056
3
546
1050
17173
8
Total
797
7377
174
546
1050
590
174
546
1050
1056
14
174
546
1050
1056
17173
2
174
546
1050
17173
1
174
546
1056
1
174
546
17173
61
174
1050
1056
106
174
1050
17173
9
546
1050
17173
13
Dortmund Data Bank Version: February 2024
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