Online DDB Search
Dortmund Data Bank
Thermophysical Data for Process Design
Contact
:
☎ +49 441 361819 0
or
✉ info@ddbst.com
⇓
Query
A quote for experimental literature data about the system can be obtained via email.
DDB#
Name
CAS-RN
Formula
8
1,2-Ethanediol
107-21-1
C
2
H
6
O
2
Overview
Details
174
Water
7732-18-5
H
2
O
Overview
Details
1050
Carbon dioxide
124-38-9
CO
2
Overview
Details
2189
2-Amino-2-methyl-1-propanol (AMP)
124-68-5
C
4
H
1
1
NO
Overview
Details
3264
Tetra-n-butylammonium bromide
1643-19-2
C
1
6
H
3
6
BrN
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
32
289
263-353 K
7-4000 kPa
8
174
1050
10
8
1050
3264
3
174
1050
2189
3
174
1050
3264
16
Gas Solubilities
GLE
171
1360
250-393 K
0-6987 kPa
8
174
1050
17
8
1050
2189
4
174
1050
2189
150
Gas Solubilities - Electrolyte Systems
EGLE
3
16
283 K (const.)
393-2129 kPa
174
1050
3264
3
Critical Data of Mixtures
CRI
3
24
279-288 K
344-2274 kPa
174
1050
3264
3
Mixture Viscosities
VIS
3
36
298-308 K
n.a.
8
174
2189
3
Mixture Surface Tensions
MSFT
10
40
288-303 K
n.a.
174
1050
3264
10
Gas Hydrate Data
GHD
79
485
241-293 K
104-25000 kPa
8
174
1050
18
174
1050
3264
61
Electrical Conductivities
ECND
12
96
298-318 K
n.a.
8
174
3264
12
Diffusion Coefficients
DIF
3
18
298 K (const.)
101 kPa (const.)
8
174
1050
2
8
1050
2189
1
Further Thermodynamic Properties
X
64
923
250-393 K
2-5200 kPa
8
174
1050
1
8
174
1050
2189
3264
13
8
174
2189
1
8
174
2189
3264
1
8
174
3264
4
174
1050
2189
44
Total
380
3287
8
174
1050
48
8
174
1050
2189
3264
13
8
174
2189
4
8
174
2189
3264
1
8
174
3264
16
8
1050
2189
5
8
1050
3264
3
174
1050
2189
197
174
1050
3264
93
Dortmund Data Bank Version: February 2024
What are "Sets" and "Points" in the Dortmund Data Bank?
© Dortmund Data Bank
by
DDBST GmbH
Online DDB search information page
Overall Statistics on Systems, Sets, and Points
Contact
Direct link to this DDB search page
(1.34 seconds)
⇑