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 23554

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H12 84.161 592-41-6 1-Hexene
2 C8H10 106.167 106-42-3 p-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]
411.38 0.00000 0.00000
408.91 0.01280 0.07650
402.51 0.04640 0.24670
398.80 0.06760 0.33380
397.03 0.07900 0.37270
392.30 0.10910 0.46930
388.40 0.13610 0.54020
381.15 0.19290 0.65470
376.99 0.23220 0.71090
373.79 0.26540 0.74920
370.17 0.30510 0.78880
367.35 0.33820 0.81690
364.28 0.38240 0.84450
358.23 0.47440 0.89210
354.94 0.53450 0.91430
349.98 0.63530 0.94340
346.79 0.70890 0.95950
343.77 0.78510 0.97320
342.02 0.83460 0.98060
339.83 0.89900 0.98890
338.05 0.95490 0.99530
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+p-Xylene
See larger image 		Vapor-Liquid Equilibrium of 1-Hexene+p-Xylene
See larger image

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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