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
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 |
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Constant Value
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 |
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Constant Value
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
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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