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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
4792
Sodium nitrate
7631-99-4
NNaO
3
Overview
Details
4911
Sodium chloride
7647-14-5
ClNa
Overview
Details
6311
Sodium sulfate
7757-82-6
Na
2
O
4
S
Overview
Details
60537
Sodium sulfate decahydrate
7727-73-3
Na
2
SO
4
*1
0
H
2
O
Overview
Details
63061
Sodium chloride dihydrate
23724-87-0
H
4
ClNaO
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
3
34
651-882 K
15789-30106 kPa
174
4911
6311
3
Heat Capacities of Mixtures, Excess Heat Capacities
CPE
2
12
298-323 K
n.a.
174
4792
4911
1
174
4911
6311
1
Solid-Liquid Equilibria
SLE
14
72
551-786 K
n.a.
4792
4911
6311
14
Vapor-Liquid Equilibria of Electrolyte Systems
ELE
55
734
278-842 K
1-22653 kPa
174
4792
4911
16
174
4911
6311
39
Densities and Volumes of Mixtures, Excess Volumes
VE
52
339
278-448 K
n.a.
174
4792
4911
5
174
4911
6311
47
Salt Solubilities
ESLE
484
2429
247-644 K
2-1,6E6 kPa
174
4792
4911
55
174
4792
4911
6311
3
174
4792
4911
6311
60537
2
174
4792
4911
6311
60537
63061
2
174
4792
4911
63061
14
174
4792
6311
12
174
4792
6311
60537
3
174
4911
6311
101
174
4911
6311
60537
72
174
4911
6311
60537
63061
8
174
4911
63061
25
174
6311
60537
187
Mixture Viscosities
VIS
13
81
298-423 K
88-101 kPa
174
4792
4911
1
174
4911
6311
12
Electrical Conductivities
ECND
2
3
298 K (const.)
88 kPa (const.)
174
4911
6311
2
Diffusion Coefficients
DIF
1
4
298 K (const.)
n.a.
174
4911
6311
1
Further Thermodynamic Properties
X
80
795
250-493 K
n.a.
174
4792
4911
6
174
4911
6311
72
174
4911
63061
1
174
6311
60537
1
Total
706
4503
174
4792
4911
84
174
4792
4911
6311
3
174
4792
4911
6311
60537
2
174
4792
4911
6311
60537
63061
2
174
4792
4911
63061
14
174
4792
6311
12
174
4792
6311
60537
3
174
4911
6311
278
174
4911
6311
60537
72
174
4911
6311
60537
63061
8
174
4911
63061
26
174
6311
60537
188
4792
4911
6311
14
Dortmund Data Bank Version: February 2024
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