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
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 |
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Constant Value
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 |
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Constant Value
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
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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