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 20442
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Data Table
| P [kPa] |
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 2955.997 |
463.67 |
0.90690 |
0.40420 |
| 2252.002 |
449.88 |
0.93420 |
0.42830 |
| 1267.001 |
423.11 |
0.96740 |
0.47450 |
| 612.000 |
394.22 |
0.98400 |
0.59970 |
| 343.000 |
373.11 |
0.98660 |
0.66720 |
(P - pressure, T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Barrufet M.A.; Liu K.; Rahman S.; Wu C.: Simultaneous Vapor - Liquid - Liquid Equilibria and Phase Molar Densities of a Quaternary System of Propane + Pentane + Octane + Water. J.Chem.Eng.Data 41 (1996) 918-922 |
Vapor-Liquid Equilibrium Data Set 23037
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 3628.462 |
0.90300 |
0.62800 |
| 3432.331 |
0.91600 |
0.64000 |
| 2941.998 |
0.94900 |
0.70700 |
| 2451.665 |
0.97600 |
0.80100 |
| 1961.332 |
0.99400 |
0.92900 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Namiot A.Yu.; Skripka V.G.; Lotter Yu.G.: Phase Equilibria in Hydrocarbon - Water Systems at High Temperatures. Viniti (1976) 1-13 |
Vapor-Liquid Equilibrium Data Set 23038
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 5226.944 |
0.78400 |
0.64000 |
| 4903.317 |
0.82100 |
0.64500 |
| 4412.997 |
0.87100 |
0.67300 |
| 3922.664 |
0.91200 |
0.71100 |
| 3432.331 |
0.94700 |
0.77000 |
| 2941.998 |
0.97700 |
0.85500 |
| 2451.665 |
0.99800 |
0.97700 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Namiot A.Yu.; Skripka V.G.; Lotter Yu.G.: Phase Equilibria in Hydrocarbon - Water Systems at High Temperatures. Viniti (1976) 1-13 |
Diagrams
List of All References
| Source |
| Namiot A.Yu.; Skripka V.G.; Lotter Yu.G.: Phase Equilibria in Hydrocarbon - Water Systems at High Temperatures. Viniti (1976) 1-13 |
| Barrufet M.A.; Liu K.; Rahman S.; Wu C.: Simultaneous Vapor - Liquid - Liquid Equilibria and Phase Molar Densities of a Quaternary System of Propane + Pentane + Octane + Water. J.Chem.Eng.Data 41 (1996) 918-922 |
Vapor-Liquid Equilibrium Data Overview
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