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 18563
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
C8H10 |
106.167 |
108-38-3 |
m-Xylene |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
| 407.95 |
0.00000 |
| 351.85 |
0.21330 |
| 351.35 |
0.40970 |
| 351.05 |
0.51090 |
| 350.75 |
0.59920 |
| 350.25 |
0.71250 |
| 349.85 |
0.80730 |
| 349.55 |
0.91320 |
| 349.85 |
1.00000 |
(T - temperature, x - liquid mole fraction)
Reference
| Source |
| Vittal Prasad T.E.; Chandrika K.; Haritha M.; Geetha N.B.; Prasad D.H.L.: Bubble temperature measurements on methanol with o-xylene and ethanol with m-xylene and p-xylene. Fluid Phase Equilib. 149 (1998) 121-125 |
Vapor-Liquid Equilibrium Data Set 32083
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
C8H10 |
106.167 |
108-38-3 |
m-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 4.264 |
0.03300 |
0.73100 |
| 6.115 |
0.13300 |
0.82100 |
| 6.706 |
0.26000 |
0.84900 |
| 6.769 |
0.27700 |
0.85900 |
| 6.966 |
0.36200 |
0.86200 |
| 7.201 |
0.56200 |
0.87700 |
| 7.289 |
0.63000 |
0.88600 |
| 7.325 |
0.65200 |
0.89100 |
| 7.559 |
0.77800 |
0.91000 |
| 7.665 |
0.84200 |
0.91600 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Kato M.: Analysis of the Excess Gibbs Energies of Binary Mixtures Using Non-Randomness Factors Determined from Excess Volume Data. Bull.Chem.Soc.Japan 55 (1982) 23-27 |
Diagrams
List of All References
| Source |
| Vittal Prasad T.E.; Chandrika K.; Haritha M.; Geetha N.B.; Prasad D.H.L.: Bubble temperature measurements on methanol with o-xylene and ethanol with m-xylene and p-xylene. Fluid Phase Equilib. 149 (1998) 121-125 |
| Kato M.: Analysis of the Excess Gibbs Energies of Binary Mixtures Using Non-Randomness Factors Determined from Excess Volume Data. Bull.Chem.Soc.Japan 55 (1982) 23-27 |
Vapor-Liquid Equilibrium Data Overview
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