Dortmund Data Bank
Vapor-Liquid Equilibrium Data
The experimental data shown in these pages are freely available and have been published already in the DDB Explorer Edition. The data represent a small sub list of all available data in the Dortmund Data Bank. For more data or any further information please search the DDB or contact DDBST.
Vapor-Liquid Equilibrium Data Set 29405
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H8O2S |
120.172 |
126-33-0 |
Sulfolane |
2 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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Constant Value
Data Table
T [K] |
x1 [mol/mol] |
334.65 |
0.00000 |
332.95 |
0.00100 |
330.95 |
0.00190 |
330.85 |
0.00210 |
329.15 |
0.00295 |
327.35 |
0.00385 |
492.65 |
0.98643 |
503.95 |
0.98931 |
516.45 |
0.99238 |
535.25 |
0.99725 |
541.45 |
0.99876 |
546.35 |
1.00000 |
(T - temperature, x - liquid mole fraction)
Reference
Source |
Mukhopadhyay M.; Pathak A.S.: Infinite-Dilution Activity Coefficients from Ebulliometric Isobaric Bubble Point-Composition Data of Hydrocarbon-Sulfolane Systems. J.Chem.Eng.Data 31 (1986) 148-152 |
Vapor-Liquid Equilibrium Data Set 29406
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H8O2S |
120.172 |
126-33-0 |
Sulfolane |
2 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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Constant Value
Data Table
T [K] |
x1 [mol/mol] |
339.25 |
0.00000 |
337.15 |
0.00100 |
335.15 |
0.00190 |
334.95 |
0.00210 |
332.75 |
0.00295 |
330.95 |
0.00385 |
504.85 |
0.98643 |
515.15 |
0.98931 |
525.75 |
0.99238 |
542.95 |
0.99725 |
548.25 |
0.99876 |
552.75 |
1.00000 |
(T - temperature, x - liquid mole fraction)
Reference
Source |
Mukhopadhyay M.; Pathak A.S.: Infinite-Dilution Activity Coefficients from Ebulliometric Isobaric Bubble Point-Composition Data of Hydrocarbon-Sulfolane Systems. J.Chem.Eng.Data 31 (1986) 148-152 |
Vapor-Liquid Equilibrium Data Set 29407
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C4H8O2S |
120.172 |
126-33-0 |
Sulfolane |
2 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
T [K] |
x1 [mol/mol] |
341.45 |
0.00000 |
339.25 |
0.00100 |
337.15 |
0.00190 |
336.95 |
0.00210 |
334.45 |
0.00295 |
332.65 |
0.00385 |
510.75 |
0.98643 |
520.65 |
0.98931 |
530.85 |
0.99238 |
546.45 |
0.99725 |
551.65 |
0.99876 |
555.65 |
1.00000 |
(T - temperature, x - liquid mole fraction)
Reference
Source |
Mukhopadhyay M.; Pathak A.S.: Infinite-Dilution Activity Coefficients from Ebulliometric Isobaric Bubble Point-Composition Data of Hydrocarbon-Sulfolane Systems. J.Chem.Eng.Data 31 (1986) 148-152 |
Diagrams
List of All References
Source |
Mukhopadhyay M.; Pathak A.S.: Infinite-Dilution Activity Coefficients from Ebulliometric Isobaric Bubble Point-Composition Data of Hydrocarbon-Sulfolane Systems. J.Chem.Eng.Data 31 (1986) 148-152 |
Vapor-Liquid Equilibrium Data Overview
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