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 33219

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H14 86.177 110-54-3 Hexane
2 C8H10 106.167 108-38-3 m-Xylene
Search the DDB for all data of this mixture

Constant Value

Pressure 101.30 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
412.20 0.00000 0.00000
401.70 0.06300 0.29500
396.40 0.09500 0.41300
388.30 0.14800 0.56600
375.80 0.24900 0.74400
371.20 0.29600 0.79800
366.30 0.35200 0.84600
355.30 0.55700 0.93200
351.10 0.67300 0.95200
348.90 0.74000 0.96300
346.90 0.81200 0.97400
344.50 0.90000 0.98300
341.50 1.00000 1.00000

(T - temperature, x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Gupta B.S.; Lee M.-J.: Isobaric Vapor–Liquid Equilibrium of Binary Systems of Hexane or Octane with 1,2-Dimethylbenzene or 1,3-Dimethylbenzene at 101.3 kPa. J.Chem.Eng.Data 57 (2012) 1237-1243

Diagrams

Vapor-Liquid Equilibrium of Hexane+m-Xylene
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Vapor-Liquid Equilibrium of Hexane+m-Xylene
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List of All References

Source
Gupta B.S.; Lee M.-J.: Isobaric Vapor–Liquid Equilibrium of Binary Systems of Hexane or Octane with 1,2-Dimethylbenzene or 1,3-Dimethylbenzene at 101.3 kPa. J.Chem.Eng.Data 57 (2012) 1237-1243

Vapor-Liquid Equilibrium Data Overview


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