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 35019
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
H2O |
18.015 |
7732-18-5 |
Water |
| 2 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 6100.005 |
0.20600 |
0.60800 |
| 7799.999 |
0.33100 |
0.63700 |
| 9599.997 |
0.46600 |
0.69500 |
| 10299.994 |
0.64000 |
0.65700 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Togo M.; Maeda T.; Ito A.; Shimoyama Y.: Measurement and correlation of phase equilibria for (water + aromatic hydrocarbon) binary mixtures at T = (573 to 623) K using microfluidic mixing. J.Chem.Thermodyn. 67 (2013) 247-252 |
Vapor-Liquid Equilibrium Data Set 35020
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
H2O |
18.015 |
7732-18-5 |
Water |
| 2 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 4299.993 |
0.07400 |
0.37100 |
| 5000.002 |
0.15100 |
0.44100 |
| 6000.000 |
0.18300 |
0.50700 |
| 6899.992 |
0.29100 |
0.51800 |
| 7699.993 |
0.30700 |
0.53800 |
| 8400.002 |
0.36300 |
0.56300 |
| 8999.993 |
0.35900 |
0.55300 |
| 9400.001 |
0.42800 |
0.55800 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Togo M.; Maeda T.; Ito A.; Shimoyama Y.: Measurement and correlation of phase equilibria for (water + aromatic hydrocarbon) binary mixtures at T = (573 to 623) K using microfluidic mixing. J.Chem.Thermodyn. 67 (2013) 247-252 |
Vapor-Liquid Equilibrium Data Set 35021
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
H2O |
18.015 |
7732-18-5 |
Water |
| 2 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 4899.997 |
0.14200 |
0.35900 |
| 5500.001 |
0.20500 |
0.42000 |
| 6399.994 |
0.26500 |
0.43300 |
| 6899.992 |
0.29600 |
0.45500 |
| 7400.005 |
0.30600 |
0.46300 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Togo M.; Maeda T.; Ito A.; Shimoyama Y.: Measurement and correlation of phase equilibria for (water + aromatic hydrocarbon) binary mixtures at T = (573 to 623) K using microfluidic mixing. J.Chem.Thermodyn. 67 (2013) 247-252 |
Diagrams
List of All References
| Source |
| Togo M.; Maeda T.; Ito A.; Shimoyama Y.: Measurement and correlation of phase equilibria for (water + aromatic hydrocarbon) binary mixtures at T = (573 to 623) K using microfluidic mixing. J.Chem.Thermodyn. 67 (2013) 247-252 |
Vapor-Liquid Equilibrium Data Overview
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