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
Search the DDB for all data of this mixture

Constant Value

Pressure 79.99 kPa

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
Search the DDB for all data of this mixture

Constant Value

Pressure 93.33 kPa

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

Pressure 99.99 kPa

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

Vapor-Liquid Equilibrium of Hexane+Sulfolane
See larger image

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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