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 480

Components

No. Formula Molar Mass CAS Registry Number Name
1 C2H3N 41.053 75-05-8 Acetonitrile
2 H2O 18.015 7732-18-5 Water
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Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
359.65 0.02900 0.26300
354.25 0.09300 0.50500
353.15 0.14200 0.55900
351.75 0.25400 0.61700
350.55 0.40200 0.65500
349.85 0.50700 0.66400
349.75 0.52700 0.67300
349.15 0.71800 0.72800
349.75 0.83900 0.78000
349.95 0.85600 0.76100
353.55 0.98600 0.94500

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

Reference

Source
Blackford D.S.; York R.: Vapor-Liquid Equilibria of the System Acrylonitrile-Acetonitrile-Water. J.Chem.Eng.Data 10 (1965) 313-318


Vapor-Liquid Equilibrium Data Set 481

Components

No. Formula Molar Mass CAS Registry Number Name
1 C2H3N 41.053 75-05-8 Acetonitrile
2 H2O 18.015 7732-18-5 Water
Search the DDB for all data of this mixture

Constant Value

Pressure 20.00 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
333.35 0.00000 0.00000
331.85 0.00300 0.06400
317.95 0.05200 0.50700
309.85 0.16800 0.73200
307.65 0.51300 0.81000
307.25 0.77200 0.83500
307.75 0.90000 0.86000
309.15 0.95500 0.91000
309.75 0.98000 0.95500
309.85 1.00000 1.00000

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

Reference

Source
Othmer D.F.; Josefowitz S.: Composition of Vapors from Boiling Binary Solutions Acetonitrile-Water System. Ind.Eng.Chem. 39 (1947) 1175-1177


Vapor-Liquid Equilibrium Data Set 482

Components

No. Formula Molar Mass CAS Registry Number Name
1 C2H3N 41.053 75-05-8 Acetonitrile
2 H2O 18.015 7732-18-5 Water
Search the DDB for all data of this mixture

Constant Value

Pressure 40.00 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
346.65 0.00800 0.10700
337.85 0.03000 0.42000
327.15 0.11800 0.68600
324.85 0.31100 0.73200
324.55 0.52000 0.74600
324.25 0.70000 0.77200
324.35 0.86000 0.80800
324.75 0.91400 0.83500
325.45 0.98000 0.91400
326.35 0.99000 0.95300

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

Reference

Source
Othmer D.F.; Josefowitz S.: Composition of Vapors from Boiling Binary Solutions Acetonitrile-Water System. Ind.Eng.Chem. 39 (1947) 1175-1177

Diagrams

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

Source
Othmer D.F.; Josefowitz S.: Composition of Vapors from Boiling Binary Solutions Acetonitrile-Water System. Ind.Eng.Chem. 39 (1947) 1175-1177
Blackford D.S.; York R.: Vapor-Liquid Equilibria of the System Acrylonitrile-Acetonitrile-Water. J.Chem.Eng.Data 10 (1965) 313-318

Vapor-Liquid Equilibrium Data Overview


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