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 3521
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
| 2 |
C8H10 |
106.167 |
108-38-3 |
m-Xylene |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
| 412.24 |
0.00000 |
| 412.17 |
0.10000 |
| 412.09 |
0.20000 |
| 412.01 |
0.30000 |
| 411.94 |
0.40000 |
| 411.88 |
0.50000 |
| 411.80 |
0.60000 |
| 411.71 |
0.70000 |
| 411.64 |
0.80000 |
| 411.56 |
0.90000 |
| 411.49 |
1.00000 |
(T - temperature, x - liquid mole fraction)
Reference
| Source |
| Kato M.; Sato T.; Hirata M.: Vapor-Liquid Equilibrium Relationship of Para-Xylene Meta-Xylene System at Atmospheric Pressure. J.Chem.Eng.Japan 4 (1971) 305-308 |
Vapor-Liquid Equilibrium Data Set 5189
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
| 2 |
C8H10 |
106.167 |
108-38-3 |
m-Xylene |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 412.25 |
0.00000 |
0.00000 |
| 412.18 |
0.10000 |
0.10180 |
| 412.10 |
0.20000 |
0.20320 |
| 412.03 |
0.30000 |
0.30420 |
| 411.95 |
0.40000 |
0.40480 |
| 411.88 |
0.50000 |
0.50500 |
| 411.80 |
0.60000 |
0.60480 |
| 411.73 |
0.70000 |
0.70420 |
| 411.65 |
0.80000 |
0.80320 |
| 411.58 |
0.90000 |
0.90180 |
| 411.50 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Zuiderweg F.J.: Recommended Test Mixtures for Distillation Columns. Recommended Test Mixtures for Distillation Columns (1969) 1-37 |
Vapor-Liquid Equilibrium Data Set 15445
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
| 2 |
C8H10 |
106.167 |
108-38-3 |
m-Xylene |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 333.25 |
0.00000 |
0.00000 |
| 333.15 |
0.08400 |
0.08700 |
| 333.10 |
0.15500 |
0.16000 |
| 333.05 |
0.24400 |
0.25100 |
| 332.95 |
0.33100 |
0.33900 |
| 332.85 |
0.40900 |
0.41900 |
| 332.80 |
0.49000 |
0.50000 |
| 332.75 |
0.57100 |
0.58000 |
| 332.65 |
0.65300 |
0.66400 |
| 332.60 |
0.73600 |
0.74600 |
| 332.50 |
0.81600 |
0.82400 |
| 332.45 |
0.89600 |
0.89900 |
| 332.40 |
0.94800 |
0.94800 |
| 332.35 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Llopis F.J.; Monton J.B.: Isobaric Vapor-Liquid Equilibria for Binary and Ternary Systems Composed of 1,4-Dimethylbenzene, 1,3-Dimethylbenzene, and 1,2-Dimethylbenzene at 6.66 and 26.66 kPa. J.Chem.Eng.Data 39 (1994) 643-646 |
Diagrams
List of All References
| Source |
| Zuiderweg F.J.: Recommended Test Mixtures for Distillation Columns. Recommended Test Mixtures for Distillation Columns (1969) 1-37 |
| Kato M.; Sato T.; Hirata M.: Vapor-Liquid Equilibrium Relationship of Para-Xylene Meta-Xylene System at Atmospheric Pressure. J.Chem.Eng.Japan 4 (1971) 305-308 |
| Llopis F.J.; Monton J.B.: Isobaric Vapor-Liquid Equilibria for Binary and Ternary Systems Composed of 1,4-Dimethylbenzene, 1,3-Dimethylbenzene, and 1,2-Dimethylbenzene at 6.66 and 26.66 kPa. J.Chem.Eng.Data 39 (1994) 643-646 |
Vapor-Liquid Equilibrium Data Overview
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