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Dortmund Data Bank
Thermophysical Data for Process Design
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DDB#
Name
CAS-RN
Formula
8
1,2-Ethanediol
107-21-1
C
2
H
6
O
2
Overview
Details
140
1-Propanol
71-23-8
C
3
H
8
O
Overview
Details
174
Water
7732-18-5
H
2
O
Overview
Details
6330
Potassium acetate
127-08-2
C
2
H
3
KO
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
55
362-404 K
101 kPa (const.)
8
140
174
3
Activity Coefficients at Infinite Dilution (Binary Solvents)
ACM
3
12
313-343 K
n.a.
8
140
6330
2
8
174
6330
1
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
2
22
297 K (const.)
n.a.
140
174
6330
2
Vapor-Liquid Equilibria of Electrolyte Systems
ELE
4
44
361-370 K
101 kPa (const.)
140
174
6330
4
Salt Solubilities
ESLE
3
27
208-270 K
n.a.
8
174
6330
3
Mixture Viscosities
VIS
3
33
298-318 K
n.a.
8
140
174
3
Mixture Surface Tensions
MSFT
1
59
293 K (const.)
n.a.
8
140
174
1
Mixture Speeds of Sound
MSOS
1
11
298 K (const.)
n.a.
8
140
174
1
Diffusion Coefficients
DIF
1
17
298 K (const.)
n.a.
8
140
174
1
Further Thermodynamic Properties
X
3
21
367-388 K
101 kPa (const.)
8
140
174
6330
3
Total
24
301
8
140
174
9
8
140
174
6330
3
8
140
6330
2
8
174
6330
4
140
174
6330
6
Dortmund Data Bank Version: February 2024
What are "Sets" and "Points" in the Dortmund Data Bank?
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