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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
60
Decane
124-18-5
C
1
0
H
2
2
Overview
Details
89
Hexane
110-54-3
C
6
H
1
4
Overview
Details
91
Heptane
142-82-5
C
7
H
1
6
Overview
Details
128
Octane
111-65-9
C
8
H
1
8
Overview
Details
174
Water
7732-18-5
H
2
O
Overview
Details
398
Nonane
111-84-2
C
9
H
2
0
Overview
Details
Search for mixtures containing this mixture as subsystem
Search data for binary subsystems
Mixture Data
Databank
Sets
Points
Temperature
Range
Pressure
Range
Activity Coefficients at Infinite Dilution (Binary Solvents)
ACM
9
45
288-308 K
n.a.
8
89
174
3
8
91
174
3
8
128
174
3
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
24
166
283-333 K
101 kPa (const.)
8
60
174
1
8
89
174
10
8
91
174
4
8
128
174
4
8
174
398
5
Solid-Liquid Equilibria
SLE
7
48
180-238 K
n.a.
60
91
128
7
Densities and Volumes of Mixtures, Excess Volumes
VE
7
58
295-311 K
97 kPa (const.)
60
89
91
1
60
89
128
1
60
91
128
3
89
91
128
1
91
128
398
1
Critical Data of Mixtures
CRI
1
39
508-569 K
2496-3033 kPa
89
91
128
1
Mixture Viscosities
VIS
1
5
293-313 K
n.a.
91
128
398
1
Mixture Surface Tensions
MSFT
6
30
298-323 K
3700-28740 kPa
60
89
174
6
Mixture Speeds of Sound
MSOS
1
15
303-333 K
6895-34477 kPa
60
91
128
398
1
Further Thermodynamic Properties
X
2
9
293-313 K
101 kPa (const.)
8
60
89
91
128
174
398
1
8
174
398
1
Total
58
415
8
60
89
91
128
174
398
1
8
60
174
1
8
89
174
13
8
91
174
7
8
128
174
7
8
174
398
6
60
89
91
1
60
89
128
1
60
89
174
6
60
91
128
10
60
91
128
398
1
89
91
128
2
91
128
398
2
Dortmund Data Bank Version: February 2024
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