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Dortmund Data Bank
Thermophysical Data for Process Design
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DDB#
Name
CAS-RN
Formula
8
1,2-Ethanediol
107-21-1
C
2
H
6
O
2
Overview
Details
91
Heptane
142-82-5
C
7
H
1
6
Overview
Details
174
Water
7732-18-5
H
2
O
Overview
Details
237
Propane
74-98-6
C
3
H
8
Overview
Details
1051
Methane
74-82-8
CH
4
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
28
336
168-378 K
140-67879 kPa
8
174
1051
16
91
237
1051
9
174
237
1051
3
Gas Solubilities
GLE
5
12
263-283 K
15000-30000 kPa
8
174
1051
5
Activity Coefficients at Infinite Dilution (Binary Solvents)
ACM
3
15
288-308 K
n.a.
8
91
174
3
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
5
23
276-333 K
101-2000 kPa
8
91
174
4
91
174
1051
1
(A)zeotropic Data
AZD
5
5
200-244 K
n.a.
91
237
1051
5
Solid-Liquid Equilibria
SLE
2
24
151-169 K
11120-31200 kPa
91
237
1051
2
Mixture Viscosities
VIS
20
255
203-473 K
3447-137910 kPa
8
174
1051
3
91
174
1051
3
91
237
1051
14
Mixture Surface Tensions
MSFT
24
222
204-365 K
14-17530 kPa
8
174
1051
10
91
237
1051
14
Mixture Thermal Conductivities
MTCN
12
135
198-424 K
4833-31543 kPa
91
237
1051
12
Mixture P-v-T Data
MPVT
30
380
151-423 K
988-35078 kPa
8
174
1051
2
91
237
1051
28
Gas Hydrate Data
GHD
123
878
229-353 K
115-1,5E6 kPa
8
174
237
7
8
174
237
1051
7
8
174
1051
35
8
237
1051
1
174
237
1051
73
Further Thermodynamic Properties
X
30
454
130-422 K
100-55261 kPa
8
91
174
237
1051
1
8
174
237
1
8
174
237
1051
2
8
174
1051
7
91
237
1051
18
174
237
1051
1
Total
287
2739
8
91
174
7
8
91
174
237
1051
1
8
174
237
8
8
174
237
1051
9
8
174
1051
78
8
237
1051
1
91
174
1051
4
91
237
1051
102
174
237
1051
77
Dortmund Data Bank Version: February 2024
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