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Dortmund Data Bank
Thermophysical Data for Process Design
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DDB#
Name
CAS-RN
Formula
39
1-Butanol
71-36-3
C
4
H
1
0
O
Overview
Details
110
Methanol
67-56-1
CH
4
O
Overview
Details
123
Naphthalene
91-20-3
C
1
0
H
8
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
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
9
251
338-390 K
99-102 kPa
39
110
140
1
39
110
174
2
39
140
174
5
110
140
174
1
Heats of Mixing
HE
4
52
293-323 K
101 kPa (const.)
39
110
174
4
Activity Coefficients at Infinite Dilution (Binary Solvents)
ACM
2
58
298 K (const.)
n.a.
39
110
174
1
110
140
174
1
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
51
493
273-378 K
99-101 kPa
39
110
174
26
39
140
174
25
(A)zeotropic Data
AZD
4
4
n.a.
99-101 kPa
39
110
174
1
39
140
174
3
Solid-Liquid Equilibria
SLE
18
334
273-349 K
n.a.
39
123
174
2
110
123
174
12
123
140
174
4
Densities and Volumes of Mixtures, Excess Volumes
VE
22
313
293-338 K
n.a.
39
110
174
10
39
140
174
3
110
123
174
2
110
140
174
7
Mixture Viscosities
VIS
1
24
303 K (const.)
n.a.
110
140
174
1
Mixture Surface Tensions
MSFT
1
20
341-364 K
101 kPa (const.)
110
140
174
1
Diffusion Coefficients
DIF
1
37
298 K (const.)
n.a.
39
110
140
1
Further Thermodynamic Properties
X
10
75
298 K (const.)
n.a.
39
110
123
140
174
1
39
110
123
174
1
39
110
174
1
39
123
174
1
110
123
140
174
1
110
123
174
2
110
140
174
1
123
140
174
2
Total
123
1661
39
110
123
140
174
1
39
110
123
174
1
39
110
140
2
39
110
174
45
39
123
174
3
39
140
174
36
110
123
140
174
1
110
123
174
16
110
140
174
12
123
140
174
6
Dortmund Data Bank Version: February 2024
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