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 8015
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
2 |
C5H9NO |
99.133 |
872-50-4 |
N-Methyl-2-pyrrolidone |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
0.012 |
0.00000 |
0.752 |
0.01430 |
1.6585 |
0.03430 |
2.709 |
0.06340 |
4.442 |
0.14410 |
5.256 |
0.24060 |
5.497 |
0.89320 |
5.577 |
0.95700 |
5.714 |
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 8016
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
2 |
C5H9NO |
99.133 |
872-50-4 |
N-Methyl-2-pyrrolidone |
Search the DDB for all data of this mixture
Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
0.020 |
0.00000 |
0.960 |
0.01430 |
2.124 |
0.03430 |
3.480 |
0.06340 |
5.774 |
0.14410 |
6.917 |
0.24060 |
7.326 |
0.36530 |
7.358 |
0.40980 |
7.374 |
0.79800 |
7.426 |
0.89320 |
7.547 |
0.95690 |
7.739 |
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 8017
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
2 |
C5H9NO |
99.133 |
872-50-4 |
N-Methyl-2-pyrrolidone |
Search the DDB for all data of this mixture
Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
0.032 |
0.00000 |
1.212 |
0.01430 |
2.684 |
0.03430 |
4.409 |
0.06330 |
7.406 |
0.14410 |
8.965 |
0.24060 |
9.609 |
0.36530 |
9.670 |
0.40870 |
9.766 |
0.67630 |
9.794 |
0.79790 |
9.887 |
0.89310 |
10.067 |
0.95690 |
10.334 |
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
List of All References
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 Overview
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