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 34209

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H14 86.177 110-54-3 Hexane
2 C2H3N 41.053 75-05-8 Acetonitrile
Search the DDB for all data of this mixture

Constant Value

Temperature 348.20 K

Data Table

P [kPa] x1 [mol/mol] y1 [mol/mol]
83.700 0.00000 0.00000
137.999 0.04200 0.47500
151.500 0.06400 0.52500
162.200 0.08100 0.56500
171.801 0.09900 0.59500
184.000 0.13200 0.62400
188.001 0.31200 0.65000
188.001 0.65400 0.65000
184.399 0.87200 0.67400
176.200 0.91600 0.71400
169.099 0.93400 0.75600
156.500 0.97100 0.81500
140.500 0.98900 0.89900
125.300 1.00000 1.00000

(P - pressure, x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Narasigadu C.; Naidoo P.; Coquelet C.; Richon D.; Ramjugernath D.: A novel static analytical apparatus for phase equilibrium measurements. Fluid Phase Equilib. 338 (2013) 188-196

Diagrams

Vapor-Liquid Equilibrium of Acetonitrile+Hexane
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Vapor-Liquid Equilibrium of Acetonitrile+Hexane
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List of All References

Source
Narasigadu C.; Naidoo P.; Coquelet C.; Richon D.; Ramjugernath D.: A novel static analytical apparatus for phase equilibrium measurements. Fluid Phase Equilib. 338 (2013) 188-196

Vapor-Liquid Equilibrium Data Overview


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