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 6609

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H6 78.114 71-43-2 Benzene
2 C8H10 106.167 108-38-3 m-Xylene
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Constant Value

Temperature 298.15 K

Data Table

P [kPa] x1 [mol/mol] y1 [mol/mol]
3.938 0.24400 0.78600
4.046 0.25200 0.79000
5.558 0.38000 0.87400
6.610 0.47000 0.90900
7.642 0.55600 0.93100
8.662 0.64500 0.95500
9.502 0.71900 0.96700
10.628 0.82000 0.98100
11.832 0.92700 0.99300

(P - pressure, x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Boublik T.; Benson G.C.: Molar Excess Gibbs Free Energies of Benzene-m-Xylene Mixtures. Can.J.Chem. 47 (1969) 539-542


Vapor-Liquid Equilibrium Data Set 6610

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H6 78.114 71-43-2 Benzene
2 C8H10 106.167 108-38-3 m-Xylene
Search the DDB for all data of this mixture

Constant Value

Temperature 310.15 K

Data Table

P [kPa] x1 [mol/mol] y1 [mol/mol]
2.944 0.03700 0.29600
3.040 0.04200 0.31400
3.609 0.07200 0.44600
3.925 0.08500 0.50100
4.877 0.13700 0.61900
7.341 0.26800 0.78200
9.821 0.39400 0.86600
11.423 0.47400 0.90000
12.634 0.53500 0.91600
14.852 0.65100 0.94800
16.679 0.74500 0.96700
18.065 0.81900 0.97700
20.092 0.92800 0.99100

(P - pressure, x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Boublik T.; Benson G.C.: Molar Excess Gibbs Free Energies of Benzene-m-Xylene Mixtures. Can.J.Chem. 47 (1969) 539-542


Vapor-Liquid Equilibrium Data Set 6611

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H6 78.114 71-43-2 Benzene
2 C8H10 106.167 108-38-3 m-Xylene
Search the DDB for all data of this mixture

Constant Value

Temperature 323.15 K

Data Table

P [kPa] x1 [mol/mol] y1 [mol/mol]
5.684 0.04400 0.30800
7.014 0.08800 0.46400
7.255 0.09500 0.48800
8.862 0.14600 0.60300
12.942 0.27400 0.76900
16.692 0.38800 0.84800
19.625 0.48000 0.89000
21.532 0.53800 0.91100
25.251 0.65400 0.94300
28.238 0.74900 0.96200
29.971 0.80400 0.97500
30.717 0.82600 0.97600

(P - pressure, x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Boublik T.; Benson G.C.: Molar Excess Gibbs Free Energies of Benzene-m-Xylene Mixtures. Can.J.Chem. 47 (1969) 539-542

Diagrams

Vapor-Liquid Equilibrium of Benzene+m-Xylene
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Vapor-Liquid Equilibrium of Benzene+m-Xylene
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List of All References

Source
Boublik T.; Benson G.C.: Molar Excess Gibbs Free Energies of Benzene-m-Xylene Mixtures. Can.J.Chem. 47 (1969) 539-542

Vapor-Liquid Equilibrium Data Overview


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