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 4024

Components

No. Formula Molar Mass CAS Registry Number Name
1 C3H6O 58.080 67-64-1 Acetone
2 C6H12 84.161 592-41-6 1-Hexene
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Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
336.75 0.00000 0.00000
331.05 0.06000 0.18400
327.85 0.11600 0.29900
326.35 0.18400 0.36500
324.65 0.28700 0.44100
323.85 0.38700 0.50000
323.35 0.49700 0.55500
323.25 0.59300 0.60500
323.25 0.60500 0.60500
323.45 0.69800 0.65800
324.15 0.80500 0.73000
325.95 0.90800 0.83800
329.55 1.00000 1.00000

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

Reference

Source
Ogorodnikov S.K.; Kogan V.B.; Nemtsov M.S.: Liquid-Vapor Equilibrium in Binary Systems of Hydrocarbons with Acetone. III.. J.Appl.Chem.USSR 34 (1961) 313-319


Vapor-Liquid Equilibrium Data Set 6506

Components

No. Formula Molar Mass CAS Registry Number Name
1 C3H6O 58.080 67-64-1 Acetone
2 C6H12 84.161 592-41-6 1-Hexene
Search the DDB for all data of this mixture

Constant Value

Temperature 293.15 K

Data Table

x1 [mol/mol] y1 [mol/mol]
0.00000 0.00000
0.05000 0.17500
0.10000 0.27600
0.20000 0.38500
0.30000 0.44500
0.40000 0.48200
0.50000 0.52200
0.60000 0.56300
0.70000 0.61700
0.80000 0.67700
0.90000 0.76600
0.95000 0.84700
1.00000 1.00000

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

Reference

Source
Lesteva T.M.; Logunova G.I.; Chernaya V.I.: Certain Physicochemical Properties of Hex-1-ene-Solvent Systems. Zh.Fiz.Khim. 53 (1979) 1180-1183


Vapor-Liquid Equilibrium Data Set 6507

Components

No. Formula Molar Mass CAS Registry Number Name
1 C3H6O 58.080 67-64-1 Acetone
2 C6H12 84.161 592-41-6 1-Hexene
Search the DDB for all data of this mixture

Constant Value

Temperature 313.15 K

Data Table

x1 [mol/mol] y1 [mol/mol]
0.00000 0.00000
0.05000 0.19500
0.10000 0.29500
0.20000 0.40700
0.30000 0.45200
0.40000 0.50600
0.50000 0.53100
0.60000 0.57400
0.70000 0.62900
0.80000 0.68700
0.90000 0.77300
0.95000 0.86000
1.00000 1.00000

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

Reference

Source
Lesteva T.M.; Logunova G.I.; Chernaya V.I.: Certain Physicochemical Properties of Hex-1-ene-Solvent Systems. Zh.Fiz.Khim. 53 (1979) 1180-1183

Diagrams

Vapor-Liquid Equilibrium of Acetone+1-Hexene
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Vapor-Liquid Equilibrium of Acetone+1-Hexene
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Vapor-Liquid Equilibrium of Acetone+1-Hexene
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List of All References

Source
Ogorodnikov S.K.; Kogan V.B.; Nemtsov M.S.: Liquid-Vapor Equilibrium in Binary Systems of Hydrocarbons with Acetone. III.. J.Appl.Chem.USSR 34 (1961) 313-319
Lesteva T.M.; Logunova G.I.; Chernaya V.I.: Certain Physicochemical Properties of Hex-1-ene-Solvent Systems. Zh.Fiz.Khim. 53 (1979) 1180-1183

Vapor-Liquid Equilibrium Data Overview


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