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 3827
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 350.85 |
0.03250 |
0.18700 |
| 349.75 |
0.04200 |
0.23000 |
| 348.80 |
0.05250 |
0.27000 |
| 346.40 |
0.08250 |
0.36000 |
| 343.85 |
0.11750 |
0.43000 |
| 338.75 |
0.24200 |
0.57000 |
| 336.55 |
0.37250 |
0.63250 |
| 335.80 |
0.45750 |
0.65750 |
| 335.30 |
0.55000 |
0.67500 |
| 335.10 |
0.61750 |
0.70000 |
| 335.05 |
0.72200 |
0.72200 |
| 335.15 |
0.81000 |
0.74750 |
| 335.55 |
0.86000 |
0.78000 |
| 337.05 |
0.95000 |
0.84750 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Govindaswamy S.; Andiappan A.; Lakshmanan S.: Isobaric Vapour-Liquid Equilibrium Data for the Ternary and Sub-Binary Systems Containing n-Hexane(1)-Benzene(2)- Isopropanol(3). J.Chem.Eng.Japan 9 (1976) 345-349 |
Vapor-Liquid Equilibrium Data Set 4789
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 345.85 |
0.04100 |
0.26000 |
| 339.35 |
0.12100 |
0.48500 |
| 335.15 |
0.22400 |
0.61000 |
| 333.35 |
0.29600 |
0.65500 |
| 332.35 |
0.41800 |
0.70600 |
| 332.25 |
0.55100 |
0.72500 |
| 332.15 |
0.65500 |
0.73000 |
| 332.25 |
0.78600 |
0.75500 |
| 333.45 |
0.90300 |
0.81100 |
| 336.25 |
0.96700 |
0.90000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Vijayaraghavan S.V.; Deshpande P.K.; Kuloor N.R.: Vapor-Liquid Equilibrium at Atmospheric Pressure (n-Hexane-2-Propanol System). Chem.Age India 15 (1964) 1267-1269 |
Vapor-Liquid Equilibrium Data Set 5021
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 350.85 |
0.02300 |
0.13600 |
| 343.20 |
0.06000 |
0.25700 |
| 341.40 |
0.11700 |
0.42400 |
| 337.85 |
0.21000 |
0.55800 |
| 337.25 |
0.24600 |
0.60000 |
| 337.05 |
0.28600 |
0.63700 |
| 335.40 |
0.39800 |
0.67200 |
| 335.35 |
0.41700 |
0.67200 |
| 335.05 |
0.49300 |
0.69100 |
| 334.70 |
0.59300 |
0.70600 |
| 334.75 |
0.65700 |
0.72000 |
| 334.70 |
0.67300 |
0.72500 |
| 334.75 |
0.72800 |
0.72700 |
| 334.95 |
0.87200 |
0.75800 |
| 335.65 |
0.92300 |
0.79900 |
| 337.05 |
0.97500 |
0.85600 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Rotter J.M.; Knickle H.N.: Isobaric Vapor-Liquid Equilibrium Data for the System n-Hexane-2-Propanol. J.Chem.Eng.Data 22 (1977) 246-248 |
Diagrams
List of All References
| Source |
| Govindaswamy S.; Andiappan A.; Lakshmanan S.: Isobaric Vapour-Liquid Equilibrium Data for the Ternary and Sub-Binary Systems Containing n-Hexane(1)-Benzene(2)- Isopropanol(3). J.Chem.Eng.Japan 9 (1976) 345-349 |
| Vijayaraghavan S.V.; Deshpande P.K.; Kuloor N.R.: Vapor-Liquid Equilibrium at Atmospheric Pressure (n-Hexane-2-Propanol System). Chem.Age India 15 (1964) 1267-1269 |
| Rotter J.M.; Knickle H.N.: Isobaric Vapor-Liquid Equilibrium Data for the System n-Hexane-2-Propanol. J.Chem.Eng.Data 22 (1977) 246-248 |
Vapor-Liquid Equilibrium Data Overview
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