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 Dortmund Data Bank
Thermophysical Data for Process Design
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Query
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DDB# Name CAS-RN Formula
142 1-Propanethiol 107-03-9 C3H8S Overview Details
174 Water 7732-18-5 H2O Overview Details
180 2-Propanethiol 75-33-2 C3H8S Overview Details
419 Ethyl methyl sulfide 624-89-5 C3H8S Overview Details
546 Monoethanolamine 141-43-5 C2H7NO Overview Details
579 Methanethiol 74-93-1 CH4S Overview Details
913 Ethanethiol 75-08-1 C2H6S Overview Details
1150 Dimethyl sulfide 75-18-3 C2H6S Overview Details
1839 Diglycolamine (DGA) 929-06-6 C4H11NO2 Overview Details
1934 n-Butylmercaptan 109-79-5 C4H10S Overview Details
1935 iso-Butylmercaptan 513-44-0 C4H10S Overview Details
2187 Methyldiethanolamine (MDEA) 105-59-9 C5H13NO2 Overview Details
3865 Piperazine 110-85-0 C4H10N2 Overview Details
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Mixture Data

Databank Sets Points Temperature
Range		 Pressure
Range
Vapor-Liquid Equilibria VLE 6 101 298-423 K2-435 kPa
174 546 2187
3
174 546 3865
2
174 2187 3865
1
Gas Solubilities GLE 50 279 293-353 Kn.a.
142 174 546
1
142 174 1839
1
142 174 2187
3
142 174 2187 3865
1
174 180 546
1
174 180 1839
1
174 180 2187
4
174 180 2187 3865
1
174 419 546
1
174 419 1839
1
174 419 2187
2
174 419 2187 3865
1
174 546 579
2
174 546 913
1
174 546 1150
1
174 546 1934
1
174 546 1935
1
174 579 1839
2
174 579 2187
3
174 579 2187 3865
1
174 913 1839
1
174 913 2187
2
174 913 2187 3865
1
174 1150 1839
1
174 1150 2187
3
174 1150 2187 3865
1
174 1839 1934
1
174 1839 1935
1
174 1934 2187
3
174 1934 2187 3865
1
174 1935 2187
4
174 1935 2187 3865
1
Activity Coefficients at Infinite Dilution (Binary Solvents) ACM 35 202 293-353 Kn.a.
142 174 546
1
142 174 1839
1
142 174 2187
3
174 180 546
1
174 180 1839
1
174 180 2187
2
174 419 546
1
174 419 1839
1
174 419 2187
2
174 546 579
1
174 546 913
1
174 546 1150
1
174 546 1934
1
174 546 1935
1
174 579 1839
1
174 579 2187
2
174 913 1839
1
174 913 2187
2
174 1150 1839
1
174 1150 2187
3
174 1839 1934
1
174 1839 1935
1
174 1934 2187
3
174 1935 2187
2
Heat Capacities of Mixtures, Excess Heat Capacities CPE 23 344 298-353 Kn.a.
174 546 2187
12
174 2187 3865
11
Solid-Liquid Equilibria SLE 1 32 253-272 Kn.a.
174 546 2187
1
Densities and Volumes of Mixtures, Excess Volumes VE 56 308 288-353 K101 kPa (const.)
174 546 2187
42
174 2187 3865
14
Mixture Viscosities VIS 61 721 288-373 K98-400 kPa
174 546 2187
23
174 546 3865
3
174 2187 3865
35
Mixture Surface Tensions MSFT 22 289 293-333 Kn.a.
174 546 2187
13
174 2187 3865
9
Mixture Thermal Conductivities MTCN 1 36 300-344 Kn.a.
174 2187 3865
1
Mixture P-v-T Data MPVT 1 4 303 K (const.)503-3990 kPa
174 2187 3865
1
Diffusion Coefficients DIF 12 36 298-368 Kn.a.
174 2187 3865
12
Further Thermodynamic Properties X 25 350 283-363 K4-13800 kPa
142 174 180 419 546 579 913 1150 1839 1934 1935 2187 3865
1
142 174 2187 3865
1
174 180 419 546 579 913 1150 1839 1934 2187 3865
1
174 180 2187 3865
1
174 419 2187 3865
1
174 546 3865
1
174 579 2187 3865
1
174 913 2187 3865
1
174 1150 2187 3865
1
174 1934 2187 3865
1
174 1935 2187 3865
1
174 2187 3865
14
Total 293 2702
142 174 180 419 546 579 913 1150 1839 1934 1935 2187 3865
1
142 174 546
2
142 174 1839
2
142 174 2187
6
142 174 2187 3865
2
174 180 419 546 579 913 1150 1839 1934 2187 3865
1
174 180 546
2
174 180 1839
2
174 180 2187
6
174 180 2187 3865
2
174 419 546
2
174 419 1839
2
174 419 2187
4
174 419 2187 3865
2
174 546 579
3
174 546 913
2
174 546 1150
2
174 546 1934
2
174 546 1935
2
174 546 2187
94
174 546 3865
6
174 579 1839
3
174 579 2187
5
174 579 2187 3865
2
174 913 1839
2
174 913 2187
4
174 913 2187 3865
2
174 1150 1839
2
174 1150 2187
6
174 1150 2187 3865
2
174 1839 1934
2
174 1839 1935
2
174 1934 2187
6
174 1934 2187 3865
2
174 1935 2187
6
174 1935 2187 3865
2
174 2187 3865
98

Dortmund Data Bank Version: February 2024
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