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 23553

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H12 84.161 592-41-6 1-Hexene
2 C8H10 106.167 108-38-3 m-Xylene
Search the DDB for all data of this mixture

Constant Value

Pressure 101.30 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
412.22 0.00000 0.00000
408.23 0.01950 0.11710
404.11 0.04030 0.22430
400.00 0.06280 0.32260
397.83 0.07630 0.37110
394.57 0.09710 0.43810
389.54 0.13110 0.53280
383.74 0.17480 0.62680
378.41 0.22180 0.70120
370.59 0.30410 0.79120
367.03 0.34760 0.82580
360.36 0.44130 0.88100
356.36 0.50870 0.90790
352.33 0.58540 0.93320
348.32 0.67280 0.95420
347.05 0.70300 0.96020
343.60 0.79040 0.97520
341.90 0.84120 0.98210
339.60 0.90740 0.99030
338.26 0.94900 0.99480
337.36 0.97790 0.99770
336.64 1.00000 1.00000

(T - temperature, x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Diaz C.; Dominguez A.; Tojo J.: Phase Equilibria of the Binary Systems 1-Hexene with ortho-Xylene, n-Xylene, p-Xylene, Toluene, ant Ethylbenzene at 101.3 kPa. J.Chem.Eng.Data 47 (2002) 867-871

Diagrams

Vapor-Liquid Equilibrium of 1-Hexene+m-Xylene
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Vapor-Liquid Equilibrium of 1-Hexene+m-Xylene
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List of All References

Source
Diaz C.; Dominguez A.; Tojo J.: Phase Equilibria of the Binary Systems 1-Hexene with ortho-Xylene, n-Xylene, p-Xylene, Toluene, ant Ethylbenzene at 101.3 kPa. J.Chem.Eng.Data 47 (2002) 867-871

Vapor-Liquid Equilibrium Data Overview


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