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Thermophysical Data for Process Design
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DDB#
Name
CAS-RN
Formula
134
Pentane
109-66-0
C
5
H
1
2
Overview
Details
237
Propane
74-98-6
C
3
H
8
Overview
Details
1051
Methane
74-82-8
CH
4
Overview
Details
1054
Ethane
74-84-0
C
2
H
6
Overview
Details
1056
Nitrogen
7727-37-9
N
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
117
1617
87-378 K
8-19049 kPa
134
237
1051
5
134
1051
1054
3
134
1051
1056
6
237
1051
1054
23
237
1051
1054
1056
38
237
1051
1056
4
237
1054
1056
3
1051
1054
1056
35
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
27
289
77-162 K
80-6313 kPa
237
1051
1054
1056
2
237
1051
1056
10
237
1054
1056
1
1051
1054
1056
14
Densities and Volumes of Mixtures, Excess Volumes
VE
1
2
108 K (const.)
n.a.
237
1051
1054
1
Critical Data of Mixtures
CRI
4
8
192-356 K
4935-10510 kPa
134
237
1051
1
134
1051
1054
1
237
1051
1054
1056
2
Mixture Viscosities
VIS
5
182
122-468 K
101-11525 kPa
237
1051
1054
2
237
1051
1054
1056
1
1051
1054
1056
2
Mixture Surface Tensions
MSFT
1
15
294 K (const.)
1502-7762 kPa
134
1051
1054
1
Mixture Dielectric Constants
MDEC
2
8
91-115 K
30-221 kPa
237
1051
1054
1
1051
1054
1056
1
Mixture P-v-T Data
MPVT
146
2756
87-500 K
8-200548 kPa
134
237
1051
22
134
237
1051
1054
1056
1
134
1051
1054
1
134
1051
1056
5
237
1051
1054
70
237
1051
1054
1056
31
237
1051
1056
2
1051
1054
1056
14
Further Thermodynamic Properties
X
97
2947
90-422 K
310-13789 kPa
237
1051
1054
67
237
1051
1054
1056
18
237
1051
1056
2
1051
1054
1056
10
Total
400
7824
134
237
1051
28
134
237
1051
1054
1056
1
134
1051
1054
6
134
1051
1056
11
237
1051
1054
164
237
1051
1054
1056
92
237
1051
1056
18
237
1054
1056
4
1051
1054
1056
76
Dortmund Data Bank Version: February 2024
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