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 15532
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
H2O |
18.015 |
7732-18-5 |
Water |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 334.05 |
0.000139 |
0.02950 |
0.00231 |
0.21000 |
| 331.75 |
0.000291 |
0.16200 |
0.00185 |
0.31100 |
| 331.45 |
0.00037 |
0.32000 |
0.00125 |
0.33900 |
| 331.45 |
0.000621 |
0.33300 |
0.00190 |
0.34000 |
| 331.35 |
0.000363 |
0.33300 |
0.00127 |
0.33900 |
| 331.55 |
0.000227 |
0.33500 |
0.000842 |
0.34300 |
| 331.25 |
0.00261 |
0.33400 |
0.00743 |
0.34100 |
| 331.55 |
0.000254 |
0.33600 |
0.000991 |
0.34300 |
| 331.45 |
0.00121 |
0.33700 |
0.00360 |
0.34300 |
| 331.65 |
0.000227 |
0.51200 |
0.000602 |
0.36600 |
| 332.65 |
0.000212 |
0.72000 |
0.00053 |
0.40700 |
| 337.85 |
0.000225 |
0.90400 |
0.000502 |
0.56000 |
| 343.25 |
0.000159 |
0.95900 |
0.000381 |
0.74100 |
| 344.25 |
0.000195 |
0.96400 |
0.000439 |
0.76500 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Ikari A.; Hatate Y.; Hosoda K.; Kawabata Y.: Vapor-Liquid Equilibria of Hexane-Acetic Acid System and Hexane-Ethanol System Containing a Minute Amount of Water. Kagaku Kogaku Ronbunshu 17 (1991) 890-894 |
Vapor-Liquid Equilibrium Data Set 29087
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 334.44 |
0.99800 |
0.00000 |
0.78600 |
0.00000 |
| 332.57 |
0.99500 |
0.00400 |
0.76500 |
0.07600 |
| 330.80 |
0.98300 |
0.01500 |
0.71100 |
0.15000 |
| 330.54 |
0.97600 |
0.02100 |
0.70200 |
0.16200 |
| 330.05 |
0.96900 |
0.02800 |
0.68800 |
0.18500 |
| 329.92 |
0.95800 |
0.03900 |
0.68100 |
0.19500 |
| 329.82 |
0.94700 |
0.04900 |
0.68000 |
0.19700 |
| 329.77 |
0.93500 |
0.06000 |
0.67600 |
0.20200 |
| 329.71 |
0.93000 |
0.06500 |
0.67300 |
0.20700 |
| 329.56 |
0.91300 |
0.08000 |
0.67000 |
0.21400 |
| 329.51 |
0.90500 |
0.08700 |
0.66500 |
0.22100 |
| 329.48 |
0.88900 |
0.10100 |
0.66300 |
0.22500 |
| 329.45 |
0.87500 |
0.11300 |
0.66100 |
0.22900 |
| 329.42 |
0.85200 |
0.13300 |
0.65800 |
0.23500 |
| 329.26 |
0.84200 |
0.14200 |
0.65700 |
0.23900 |
| 329.28 |
0.80600 |
0.17200 |
0.65600 |
0.24200 |
| 329.48 |
0.76800 |
0.20300 |
0.65300 |
0.24600 |
| 329.50 |
0.72800 |
0.23500 |
0.65300 |
0.24800 |
| 329.53 |
0.68000 |
0.27200 |
0.65200 |
0.25300 |
| 329.55 |
0.64800 |
0.29700 |
0.65000 |
0.25400 |
| 329.56 |
0.62200 |
0.31600 |
0.64900 |
0.25600 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Gomis V.; Font A.; Pedraza R.; Saquete M.D.: Isobaric vapor-liquid and vapor-liquid-liquid equilibrium data for the water-ethanol-hexane system. Fluid Phase Equilib. 259 (2007) 66-70 |
Comment: VLLE, organic phase
Vapor-Liquid Equilibrium Data Set 29088
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 332.57 |
0.00000 |
0.03500 |
0.76500 |
0.07600 |
| 330.80 |
0.00100 |
0.10600 |
0.71100 |
0.15000 |
| 330.54 |
0.00100 |
0.13100 |
0.70200 |
0.16200 |
| 330.05 |
0.00100 |
0.20800 |
0.68800 |
0.18500 |
| 329.92 |
0.00200 |
0.24400 |
0.68100 |
0.19500 |
| 329.82 |
0.00200 |
0.26600 |
0.68000 |
0.19700 |
| 329.77 |
0.00300 |
0.29300 |
0.67600 |
0.20200 |
| 329.71 |
0.00400 |
0.32200 |
0.67300 |
0.20700 |
| 329.56 |
0.00800 |
0.37600 |
0.67000 |
0.21400 |
| 329.51 |
0.01200 |
0.43300 |
0.66500 |
0.22100 |
| 329.48 |
0.01400 |
0.46100 |
0.66300 |
0.22500 |
| 329.45 |
0.01900 |
0.49200 |
0.66100 |
0.22900 |
| 329.42 |
0.02900 |
0.54100 |
0.65800 |
0.23500 |
| 329.26 |
0.04600 |
0.57500 |
0.65700 |
0.23900 |
| 329.28 |
0.05300 |
0.59300 |
0.65600 |
0.24200 |
| 329.48 |
0.06300 |
0.61300 |
0.65300 |
0.24600 |
| 329.50 |
0.07900 |
0.62400 |
0.65300 |
0.24800 |
| 329.53 |
0.13200 |
0.62000 |
0.65200 |
0.25300 |
| 329.55 |
0.15700 |
0.60900 |
0.65000 |
0.25400 |
| 329.56 |
0.17800 |
0.60400 |
0.64900 |
0.25600 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Gomis V.; Font A.; Pedraza R.; Saquete M.D.: Isobaric vapor-liquid and vapor-liquid-liquid equilibrium data for the water-ethanol-hexane system. Fluid Phase Equilib. 259 (2007) 66-70 |
Comment: VLLE, aqueous phase
List of All References
Vapor-Liquid Equilibrium Data Overview
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