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 15334
Components
| No. | Formula | Molar Mass | CAS Registry Number | Name |
|---|---|---|---|---|
| 1 | H2O | 18.015 | 7732-18-5 | Water |
| 2 | C8H10 | 106.167 | 108-38-3 | m-Xylene |
Constant Value
| Pressure | 101.30 | kPa |
|---|
Data Table
| T [K] | x1 [mol/mol] | y1 [mol/mol] |
|---|---|---|
| 408.15 | 0.00220 | 0.12160 |
| 407.59 | 0.00290 | 0.13960 |
| 405.01 | 0.00350 | 0.18750 |
| 399.85 | 0.00820 | 0.30820 |
| 395.63 | 0.01220 | 0.40130 |
| 391.15 | 0.01630 | 0.48070 |
| 385.91 | 0.02420 | 0.56270 |
| 382.35 | 0.02310 | 0.60230 |
| 377.35 | 0.03490 | 0.67040 |
| 374.89 | 0.08640 | 0.69210 |
| 372.65 | 0.12940 | 0.71260 |
| 370.25 | 0.20570 | 0.72430 |
| 369.87 | 0.24350 | 0.73780 |
| 367.16 | 0.99920 | 0.79240 |
| 367.20 | 0.99928 | 0.79920 |
| 367.46 | 0.99940 | 0.81380 |
| 368.06 | 0.99957 | 0.83130 |
| 369.32 | 0.99980 | 0.87230 |
| 371.21 | 0.99993 | 0.93340 |
| 372.84 | 0.99999 | 0.98970 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
|---|
| Tu M.; Lai G.; Fei D.: Vapor-Liquid Phase Equilibrium of Binary System of Benzene-Water and m-Xylene-Water. Huagong-Xuebao / CIESC J. 45 (1994) 225-229 |
Diagrams
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List of All References
| Source |
|---|
| Tu M.; Lai G.; Fei D.: Vapor-Liquid Phase Equilibrium of Binary System of Benzene-Water and m-Xylene-Water. Huagong-Xuebao / CIESC J. 45 (1994) 225-229 |
Vapor-Liquid Equilibrium Data Overview