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 8824
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
60-29-7 |
Diethyl ether |
| 2 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 341.84 |
0.00000 |
0.00000 |
| 337.82 |
0.04280 |
0.15300 |
| 335.36 |
0.08390 |
0.25050 |
| 330.93 |
0.16360 |
0.38180 |
| 326.49 |
0.26210 |
0.54230 |
| 321.71 |
0.38290 |
0.66170 |
| 318.34 |
0.49560 |
0.75530 |
| 315.68 |
0.59670 |
0.81960 |
| 313.62 |
0.67590 |
0.85790 |
| 311.74 |
0.77530 |
0.90530 |
| 309.95 |
0.86100 |
0.93920 |
| 308.79 |
0.92600 |
0.96430 |
| 308.28 |
0.95320 |
0.97820 |
| 307.99 |
0.97020 |
0.98510 |
| 307.74 |
0.98360 |
0.99120 |
| 307.63 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Klon-Palczewska M.; Cholinski J.; Wyrzykowska-Stankiewicz D.: Isobaric Vapour-Liquid Equilibrium in Binary Organic Solvent Mixtures. Chem.Stosow. 24 (1980) 197-209 |
Vapor-Liquid Equilibrium Data Set 9769
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
60-29-7 |
Diethyl ether |
| 2 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 341.85 |
0.00000 |
0.00000 |
| 340.14 |
0.01800 |
0.09290 |
| 337.83 |
0.06070 |
0.21480 |
| 335.58 |
0.08090 |
0.26540 |
| 334.96 |
0.10090 |
0.30830 |
| 329.70 |
0.19940 |
0.43770 |
| 326.26 |
0.30380 |
0.55000 |
| 322.55 |
0.42430 |
0.68470 |
| 319.61 |
0.50020 |
0.74230 |
| 316.49 |
0.59920 |
0.82980 |
| 314.37 |
0.69400 |
0.87780 |
| 311.98 |
0.79890 |
0.93790 |
| 309.22 |
0.89940 |
0.96790 |
| 308.93 |
0.91920 |
0.97630 |
| 308.81 |
0.93670 |
0.98060 |
| 308.53 |
0.95520 |
0.98600 |
| 308.11 |
0.97560 |
0.99330 |
| 307.75 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Goloborodkina R.V.; Beregovykh V.V.; Babich S.V.; Timofeev V.S.; Lvov S.V.: Dampf-Flüssig-Gleichgewicht in den Systemen Diethylester-Aceton, Diethylester-Hexan, Diethylester-Methanol bei Atmosphärendruck. Khim.-Farm.Zh. 15 (1981) 79-83 |
Diagrams
List of All References
| Source |
| Klon-Palczewska M.; Cholinski J.; Wyrzykowska-Stankiewicz D.: Isobaric Vapour-Liquid Equilibrium in Binary Organic Solvent Mixtures. Chem.Stosow. 24 (1980) 197-209 |
| Goloborodkina R.V.; Beregovykh V.V.; Babich S.V.; Timofeev V.S.; Lvov S.V.: Dampf-Flüssig-Gleichgewicht in den Systemen Diethylester-Aceton, Diethylester-Hexan, Diethylester-Methanol bei Atmosphärendruck. Khim.-Farm.Zh. 15 (1981) 79-83 |
Vapor-Liquid Equilibrium Data Overview
© DDBST GmbH
