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 477
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 27.778 |
0.00000 |
0.00000 |
| 30.038 |
0.04270 |
0.10840 |
| 32.331 |
0.10280 |
0.21310 |
| 34.372 |
0.18550 |
0.30870 |
| 35.792 |
0.27940 |
0.38430 |
| 36.778 |
0.40540 |
0.46250 |
| 36.978 |
0.45420 |
0.49020 |
| 37.068 |
0.49310 |
0.51150 |
| 36.996 |
0.60200 |
0.57260 |
| 36.457 |
0.70910 |
0.63930 |
| 35.285 |
0.81710 |
0.72170 |
| 33.553 |
0.90600 |
0.81820 |
| 31.957 |
0.95450 |
0.89440 |
| 29.819 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Brown I.; Smith F.: VI The Systems Acetonitrile + Benzene at 45°C and Acetonitrile + Nitromethane at 60°C. Aust.J.Chem. 8 (1955) 62-67 |
Vapor-Liquid Equilibrium Data Set 1624
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 9.799 |
0.01800 |
0.05400 |
| 10.106 |
0.03300 |
0.09600 |
| 10.599 |
0.06300 |
0.16100 |
| 10.639 |
0.06400 |
0.16200 |
| 11.106 |
0.09800 |
0.22100 |
| 11.386 |
0.12800 |
0.25600 |
| 11.719 |
0.16800 |
0.30000 |
| 11.852 |
0.18700 |
0.32100 |
| 11.932 |
0.19800 |
0.33000 |
| 12.186 |
0.24300 |
0.37000 |
| 12.226 |
0.25600 |
0.37600 |
| 12.359 |
0.28400 |
0.39500 |
| 12.439 |
0.31000 |
0.41200 |
| 12.466 |
0.32000 |
0.41700 |
| 12.612 |
0.36800 |
0.44200 |
| 12.666 |
0.42400 |
0.47300 |
| 12.679 |
0.43500 |
0.47900 |
| 12.679 |
0.44600 |
0.48400 |
| 12.692 |
0.44600 |
0.48600 |
| 12.719 |
0.47000 |
0.49800 |
| 12.692 |
0.48100 |
0.50100 |
| 12.746 |
0.51100 |
0.51800 |
| 12.732 |
0.51200 |
0.51900 |
| 12.746 |
0.53500 |
0.53200 |
| 12.719 |
0.57200 |
0.55100 |
| 12.719 |
0.60700 |
0.57100 |
| 12.666 |
0.64800 |
0.59300 |
| 12.639 |
0.65700 |
0.59700 |
| 12.612 |
0.67900 |
0.61200 |
| 12.519 |
0.71000 |
0.63200 |
| 12.359 |
0.75300 |
0.66200 |
| 12.186 |
0.79300 |
0.69500 |
| 12.119 |
0.81500 |
0.70900 |
| 12.012 |
0.84100 |
0.73400 |
| 11.866 |
0.85700 |
0.75700 |
| 11.706 |
0.87400 |
0.76700 |
| 11.386 |
0.90600 |
0.80800 |
| 11.252 |
0.92000 |
0.82900 |
| 11.106 |
0.93300 |
0.84900 |
| 11.026 |
0.93900 |
0.86000 |
| 10.879 |
0.95300 |
0.88300 |
| 10.692 |
0.96600 |
0.90600 |
| 10.506 |
0.97500 |
0.93000 |
| 10.319 |
0.98300 |
0.95000 |
| 10.186 |
0.99100 |
0.97200 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Werner G.; Schuberth H.: Das Phasengleichgewicht flüssig-flüssig des Systems Benzol/n-Heptan/Acetonitril sowie die Phasengleichgewichte dampfförmig-flüssig der entsprechenden binären Systeme bei 20,0°C. J.Prakt.Chem. 31 (1966) 225-239 |
Vapor-Liquid Equilibrium Data Set 1992
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 28.851 |
0.01670 |
0.04840 |
| 32.651 |
0.10880 |
0.22510 |
| 34.784 |
0.20470 |
0.32410 |
| 36.157 |
0.31420 |
0.40130 |
| 37.010 |
0.43200 |
0.48540 |
| 37.157 |
0.47340 |
0.50380 |
| 37.117 |
0.58550 |
0.56390 |
| 36.664 |
0.69090 |
0.63300 |
| 35.810 |
0.77790 |
0.69820 |
| 33.131 |
0.92560 |
0.84690 |
| 31.251 |
0.97530 |
0.93180 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Palmer D.A.; Smith B.D.: Thermodynamic Excess Property Measurements for Acetonitrile-Benzene-n-Heptane System at 45°C. J.Chem.Eng.Data 17 (1972) 71-76 |
Diagrams
List of All References
| Source |
| Brown I.; Smith F.: VI The Systems Acetonitrile + Benzene at 45°C and Acetonitrile + Nitromethane at 60°C. Aust.J.Chem. 8 (1955) 62-67 |
| Werner G.; Schuberth H.: Das Phasengleichgewicht flüssig-flüssig des Systems Benzol/n-Heptan/Acetonitril sowie die Phasengleichgewichte dampfförmig-flüssig der entsprechenden binären Systeme bei 20,0°C. J.Prakt.Chem. 31 (1966) 225-239 |
| Palmer D.A.; Smith B.D.: Thermodynamic Excess Property Measurements for Acetonitrile-Benzene-n-Heptane System at 45°C. J.Chem.Eng.Data 17 (1972) 71-76 |
Vapor-Liquid Equilibrium Data Overview
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