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Thermophysical Data for Process Design
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DDB#
Name
CAS-RN
Formula
4
Acetone
67-64-1
C
3
H
6
O
Overview
Details
11
Ethanol
64-17-5
C
2
H
6
O
Overview
Details
39
1-Butanol
71-36-3
C
4
H
1
0
O
Overview
Details
174
Water
7732-18-5
H
2
O
Overview
Details
379
2-Ethyl-1-hexanol
104-76-7
C
8
H
1
8
O
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
23
521
303-473 K
12-2471 kPa
4
11
39
2
4
11
174
3
4
39
174
1
11
39
174
14
11
39
379
1
11
174
379
1
39
174
379
1
Heats of Mixing
HE
5
62
293-323 K
101 kPa (const.)
4
11
174
1
4
39
174
4
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
77
765
256-473 K
100-200000 kPa
4
11
39
174
1
4
11
39
174
379
1
4
39
174
16
4
174
379
5
11
39
174
34
11
174
379
12
39
174
379
8
(A)zeotropic Data
AZD
5
5
323 K (const.)
8-102 kPa
4
11
39
1
4
11
174
1
11
39
174
2
39
174
379
1
Solid-Liquid Equilibria
SLE
1
10
277-288 K
n.a.
4
11
174
1
Densities and Volumes of Mixtures, Excess Volumes
VE
11
323
283-353 K
n.a.
4
39
174
2
11
39
174
9
Mixture Viscosities
VIS
6
72
298-343 K
n.a.
4
11
39
1
4
11
174
5
Mixture Surface Tensions
MSFT
2
9
303-343 K
n.a.
4
11
39
1
4
11
174
1
Mixture Thermal Conductivities
MTCN
8
233
293-353 K
n.a.
4
39
174
1
11
39
174
7
Mixture P-v-T Data
MPVT
12
140
373-473 K
60-2471 kPa
11
39
174
3
11
39
379
3
11
174
379
3
39
174
379
3
Mixture Flash Points
MFLP
4
87
289-317 K
n.a.
11
39
174
4
Further Thermodynamic Properties
X
1
20
n.a.
n.a.
4
11
39
1
Total
155
2247
4
11
39
6
4
11
39
174
1
4
11
39
174
379
1
4
11
174
12
4
39
174
24
4
174
379
5
11
39
174
73
11
39
379
4
11
174
379
16
39
174
379
13
Dortmund Data Bank Version: February 2024
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