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Thermophysical Data for Process Design
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DDB#
Name
CAS-RN
Formula
11
Ethanol
64-17-5
C
2
H
6
O
Overview
Details
21
Ethyl acetate
141-78-6
C
4
H
8
O
2
Overview
Details
84
Acetic acid
64-19-7
C
2
H
4
O
2
Overview
Details
174
Water
7732-18-5
H
2
O
Overview
Details
23990
1-Ethyl-3-methylimidazolium hydrogensulfate
412009-61-1
C
6
H
1
2
N
2
O
4
S
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
25
934
313-391 K
19-137 kPa
11
21
84
174
4
11
21
174
19
21
84
174
2
Heats of Mixing
HE
3
56
298-313 K
100-101 kPa
11
21
84
1
11
21
84
174
2
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
136
1571
273-351 K
100-101 kPa
11
21
84
174
26
11
21
174
58
11
21
23990
3
21
84
174
47
21
84
23990
2
(A)zeotropic Data
AZD
20
20
272-362 K
3-193 kPa
11
21
174
19
11
84
174
1
Densities and Volumes of Mixtures, Excess Volumes
VE
25
949
288-343 K
101 kPa (const.)
11
21
174
19
11
21
23990
1
11
84
174
2
21
84
174
2
21
84
23990
1
Critical Data of Mixtures
CRI
2
12
293-553 K
101-7440 kPa
11
21
84
174
2
Mixture Viscosities
VIS
5
243
298-318 K
101 kPa (const.)
11
21
174
2
11
84
174
3
Mixture Speeds of Sound
MSOS
15
510
288-323 K
101 kPa (const.)
11
21
174
15
Mixture Thermal Conductivities
MTCN
3
18
293-333 K
n.a.
11
21
174
3
Diffusion Coefficients
DIF
6
24
288-318 K
n.a.
11
84
174
6
Further Thermodynamic Properties
X
10
242
295-343 K
101 kPa (const.)
11
21
84
174
7
11
21
84
174
23990
1
11
84
174
1
21
84
174
1
Total
250
4579
11
21
84
1
11
21
84
174
41
11
21
84
174
23990
1
11
21
174
135
11
21
23990
4
11
84
174
13
21
84
174
52
21
84
23990
3
Dortmund Data Bank Version: February 2024
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