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 1416

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H6 78.114 71-43-2 Benzene
2 C5H9NO 99.133 872-50-4 N-Methyl-2-pyrrolidone
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Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
423.45 0.09000 0.72500
396.85 0.20000 0.86500
384.05 0.32500 0.92500
376.15 0.46500 0.93000
373.65 0.50000 0.94000
367.15 0.60000 0.94000
364.45 0.67000 0.94500

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

Reference

Source
Zaretskii M.I.; Kogan V.B.; Kononov N.F.; Podolyak V.G.: Liquid-Vapor Equilibrium in Systems Formed by Thiopene and Benzene with N,N-Dimethylformamide and N-Methylpyrrolidone. J.Appl.Chem.USSR 44 (1971) 583-588


Vapor-Liquid Equilibrium Data Set 8018

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H6 78.114 71-43-2 Benzene
2 C5H9NO 99.133 872-50-4 N-Methyl-2-pyrrolidone
Search the DDB for all data of this mixture

Constant Value

Temperature 281.15 K

Data Table

P [kPa] x1 [mol/mol]
0.012 0.00000
0.26265 0.04700
0.472 0.08760
0.7333 0.13460
1.524 0.27520
2.209 0.39430
2.9824 0.52630
3.4224 0.60280
4.345 0.77090
4.810 0.86430
5.100 0.92640
5.186 0.94540
5.321 0.97310
5.462 1.00000

(P - pressure, x - liquid mole fraction)

Reference

Source
Aim K.: Measurement of Vapor-Liquid Equilibrium in Systems with Components of Very Different Volatility by the Total Pressure Static Method. Fluid Phase Equilib. 2 (1978) 119-142


Vapor-Liquid Equilibrium Data Set 8019

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H6 78.114 71-43-2 Benzene
2 C5H9NO 99.133 872-50-4 N-Methyl-2-pyrrolidone
Search the DDB for all data of this mixture

Constant Value

Temperature 287.15 K

Data Table

P [kPa] x1 [mol/mol]
0.020 0.00000
0.36264 0.04700
0.6586 0.08760
1.012 0.13450
2.097 0.27510
3.037 0.39430
4.089 0.52630
4.680 0.60240
5.929 0.77080
6.558 0.86430
6.963 0.92640
7.082 0.94540
7.263 0.97310
7.457 1.00000

(P - pressure, x - liquid mole fraction)

Reference

Source
Aim K.: Measurement of Vapor-Liquid Equilibrium in Systems with Components of Very Different Volatility by the Total Pressure Static Method. Fluid Phase Equilib. 2 (1978) 119-142

Diagrams

Vapor-Liquid Equilibrium of Benzene+N-Methyl-2-pyrrolidone
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Vapor-Liquid Equilibrium of Benzene+N-Methyl-2-pyrrolidone
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Vapor-Liquid Equilibrium of Benzene+N-Methyl-2-pyrrolidone
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List of All References

Source
Zaretskii M.I.; Kogan V.B.; Kononov N.F.; Podolyak V.G.: Liquid-Vapor Equilibrium in Systems Formed by Thiopene and Benzene with N,N-Dimethylformamide and N-Methylpyrrolidone. J.Appl.Chem.USSR 44 (1971) 583-588
Aim K.: Measurement of Vapor-Liquid Equilibrium in Systems with Components of Very Different Volatility by the Total Pressure Static Method. Fluid Phase Equilib. 2 (1978) 119-142

Vapor-Liquid Equilibrium Data Overview


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