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Thermophysical Data for Process Design
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DDB#
Name
CAS-RN
Formula
95
2-Propanol
67-63-0
C
3
H
8
O
Overview
Details
174
Water
7732-18-5
H
2
O
Overview
Details
1050
Carbon dioxide
124-38-9
CO
2
Overview
Details
4911
Sodium chloride
7647-14-5
ClNa
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
151
293-373 K
1020-39448 kPa
95
174
1050
12
174
1050
4911
15
Gas Solubilities
GLE
4
50
283-313 K
101 kPa (const.)
95
174
1050
4
Gas Solubilities - Electrolyte Systems
EGLE
249
1800
268-723 K
4-140000 kPa
174
1050
4911
249
Activity Coefficients at Infinite Dilution (Binary Solvents)
ACM
4
16
303-333 K
n.a.
95
174
4911
4
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
40
267
288-354 K
101-36020 kPa
95
174
1050
27
95
174
4911
12
174
1050
4911
1
Vapor-Liquid Equilibria of Electrolyte Systems
ELE
21
184
318-423 K
51-40040 kPa
95
174
4911
10
174
1050
4911
11
Densities and Volumes of Mixtures, Excess Volumes
VE
9
42
283-313 K
n.a.
95
174
4911
9
Salt Solubilities
ESLE
11
96
255-308 K
n.a.
95
174
4911
11
Mixture Viscosities
VIS
37
150
273-448 K
2070-100100 kPa
95
174
4911
6
174
1050
4911
31
Mixture Surface Tensions
MSFT
114
1690
288-423 K
100-69510 kPa
95
174
1050
2
174
1050
4911
112
Mixture P-v-T Data
MPVT
70
621
275-773 K
2070-226900 kPa
95
174
1050
3
174
1050
4911
67
Gas Hydrate Data
GHD
70
490
251-285 K
275-60140 kPa
95
174
1050
15
95
174
1050
4911
7
174
1050
4911
48
Electrical Conductivities
ECND
9
161
298 K (const.)
n.a.
95
174
4911
9
Diffusion Coefficients
DIF
8
41
288-323 K
101-30000 kPa
174
1050
4911
8
Further Thermodynamic Properties
X
90
1558
268-673 K
101-40000 kPa
95
174
1050
4
95
174
4911
10
174
1050
4911
76
Total
763
7317
95
174
1050
67
95
174
1050
4911
7
95
174
4911
71
174
1050
4911
618
Dortmund Data Bank Version: February 2024
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