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Thermophysical Data for Process Design
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DDB#
Name
CAS-RN
Formula
50
Cyclohexane
110-82-7
C
6
H
1
2
Overview
Details
53
Methylcyclohexane
108-87-2
C
7
H
1
4
Overview
Details
60
Decane
124-18-5
C
1
0
H
2
2
Overview
Details
78
Dodecane
112-40-3
C
1
2
H
2
6
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
134
Pentane
109-66-0
C
5
H
1
2
Overview
Details
388
Tridecane
629-50-5
C
1
3
H
2
8
Overview
Details
398
Nonane
111-84-2
C
9
H
2
0
Overview
Details
401
Ethylcyclohexane
1678-91-7
C
8
H
1
6
Overview
Details
724
n-Undecane
1120-21-4
C
1
1
H
2
4
Overview
Details
1050
Carbon dioxide
124-38-9
CO
2
Overview
Details
1051
Methane
74-82-8
CH
4
Overview
Details
1543
n-Propyl cyclohexane
1678-92-8
C
9
H
1
8
Overview
Details
1917
n-Butylcyclohexane
1678-93-9
C
1
0
H
2
0
Overview
Details
2223
Heptylcyclohexane
5617-41-4
C
1
3
H
2
6
Overview
Details
7961
Hexylcyclohexane
4292-75-5
C
1
2
H
2
4
Overview
Details
8709
n-Pentylcyclohexane
4292-92-6
C
1
1
H
2
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
37
425
258-470 K
101-25693 kPa
50
89
91
1
50
89
1050
4
50
89
1051
4
50
91
1051
1
60
89
1050
3
60
89
1051
3
60
128
1050
3
60
724
1050
1
60
1050
1051
1
78
724
1050
1
91
134
1050
3
91
1050
1051
4
128
134
1050
5
134
1050
1051
3
Heats of Mixing
HE
2
118
298 K (const.)
n.a.
50
78
89
1
50
89
128
1
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
3
280
175-204 K
2652-5898 kPa
89
128
1051
1
89
1050
1051
1
128
134
1051
1
Solid-Liquid Equilibria
SLE
7
48
180-238 K
n.a.
60
91
128
7
Densities and Volumes of Mixtures, Excess Volumes
VE
40
988
293-348 K
97-40000 kPa
50
53
89
1
50
53
91
1
50
53
128
1
50
60
91
1
50
89
91
1
50
91
128
1
50
91
398
1
60
78
91
128
3
60
89
91
1
60
89
128
1
60
91
128
3
78
89
128
1
78
89
398
1
89
91
128
1
89
91
134
17
91
128
388
724
4
91
128
398
1
Critical Data of Mixtures
CRI
2
46
493-569 K
2496-3033 kPa
89
91
128
1
89
91
134
1
Mixture Viscosities
VIS
47
600
293-401 K
101-24626 kPa
50
89
91
1
60
89
91
134
1
60
89
91
134
1050
2
60
128
134
36
60
134
1050
2
91
128
388
724
4
91
128
398
1
Mixture Surface Tensions
MSFT
2
15
323 K (const.)
100-12800 kPa
91
1050
1051
2
Mixture Speeds of Sound
MSOS
5
57
298-333 K
6895-34477 kPa
50
89
91
1
60
91
128
398
1
89
134
1051
3
Mixture P-v-T Data
MPVT
34
966
169-363 K
2203-70000 kPa
50
91
1051
1
78
91
1050
16
89
128
1051
4
89
1050
1051
5
128
134
1051
4
128
1050
1051
4
Further Thermodynamic Properties
X
6
76
233-343 K
100-10342 kPa
50
53
60
78
89
91
128
134
388
398
401
724
1050
1051
1543
1917
2223
7961
8709
1
60
78
89
1
128
1050
1051
4
Total
185
3619
50
53
60
78
89
91
128
134
388
398
401
724
1050
1051
1543
1917
2223
7961
8709
1
50
53
89
1
50
53
91
1
50
53
128
1
50
60
91
1
50
78
89
1
50
89
91
4
50
89
128
1
50
89
1050
4
50
89
1051
4
50
91
128
1
50
91
398
1
50
91
1051
2
60
78
89
1
60
78
91
128
3
60
89
91
1
60
89
91
134
1
60
89
91
134
1050
2
60
89
128
1
60
89
1050
3
60
89
1051
3
60
91
128
10
60
91
128
398
1
60
128
134
36
60
128
1050
3
60
134
1050
2
60
724
1050
1
60
1050
1051
1
78
89
128
1
78
89
398
1
78
91
1050
16
78
724
1050
1
89
91
128
2
89
91
134
18
89
128
1051
5
89
134
1051
3
89
1050
1051
6
91
128
388
724
8
91
128
398
2
91
134
1050
3
91
1050
1051
6
128
134
1050
5
128
134
1051
5
128
1050
1051
8
134
1050
1051
3
Dortmund Data Bank Version: February 2024
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