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 5577
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 2 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 408.65 |
0.01000 |
0.09500 |
| 402.40 |
0.03000 |
0.25000 |
| 403.65 |
0.03250 |
0.21750 |
| 390.65 |
0.08000 |
0.45500 |
| 386.25 |
0.11250 |
0.52500 |
| 381.79 |
0.13500 |
0.57000 |
| 376.10 |
0.16750 |
0.62000 |
| 373.15 |
0.21000 |
0.68000 |
| 367.74 |
0.31250 |
0.77800 |
| 362.05 |
0.44250 |
0.84500 |
| 361.15 |
0.51000 |
0.87200 |
| 358.65 |
0.64000 |
0.89500 |
| 357.65 |
0.73000 |
0.91500 |
| 357.39 |
0.77250 |
0.91250 |
| 356.65 |
0.82250 |
0.93000 |
| 356.23 |
0.85750 |
0.93500 |
| 355.97 |
0.88000 |
0.94400 |
| 355.58 |
0.92100 |
0.95500 |
| 355.26 |
0.95250 |
0.96750 |
| 355.06 |
0.96250 |
0.97250 |
| 354.96 |
0.97750 |
0.98250 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Bagga O.P.; Katyal R.C.; Raju K.S.N.: Acetonitrile-Ethylbenzene and Acetonitrile-p-Xylene. J.Chem.Eng.Data 22 (1977) 416-418 |
Vapor-Liquid Equilibrium Data Set 14179
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 2 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 368.95 |
0.00000 |
0.00000 |
| 366.85 |
0.00800 |
0.08300 |
| 363.85 |
0.01700 |
0.17500 |
| 360.65 |
0.02500 |
0.25800 |
| 359.85 |
0.02600 |
0.27800 |
| 356.25 |
0.03800 |
0.36000 |
| 352.25 |
0.05300 |
0.44500 |
| 349.85 |
0.06300 |
0.49700 |
| 346.65 |
0.07500 |
0.55500 |
| 342.65 |
0.10000 |
0.62000 |
| 338.85 |
0.12800 |
0.68500 |
| 336.25 |
0.15800 |
0.72500 |
| 332.35 |
0.20700 |
0.77000 |
| 331.55 |
0.22000 |
0.78300 |
| 330.65 |
0.24000 |
0.79500 |
| 329.55 |
0.25500 |
0.80500 |
| 327.55 |
0.31800 |
0.83000 |
| 324.55 |
0.45800 |
0.85500 |
| 322.15 |
0.58800 |
0.89000 |
| 321.15 |
0.67800 |
0.91500 |
| 320.55 |
0.73800 |
0.92400 |
| 319.95 |
0.79500 |
0.93500 |
| 319.55 |
0.83000 |
0.94300 |
| 318.95 |
0.90400 |
0.95800 |
| 317.75 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Di Cave S.; Mazzarotta B.: Isobaric Vapor-Liquid Equilibria for the Binary Systems Formed by Acetonitrile and Aromatic Hydrocarbons. J.Chem.Eng.Data 36 (1991) 293-297 |
Vapor-Liquid Equilibrium Data Set 14180
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 2 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 411.15 |
0.00000 |
0.00000 |
| 409.25 |
0.01000 |
0.04600 |
| 408.25 |
0.01500 |
0.09000 |
| 406.85 |
0.02000 |
0.12500 |
| 405.15 |
0.02200 |
0.14100 |
| 403.95 |
0.02700 |
0.17300 |
| 402.55 |
0.03300 |
0.20200 |
| 400.15 |
0.04500 |
0.27000 |
| 396.25 |
0.06000 |
0.35500 |
| 394.25 |
0.06300 |
0.40300 |
| 390.55 |
0.07800 |
0.46000 |
| 389.15 |
0.09400 |
0.49500 |
| 385.55 |
0.10700 |
0.55500 |
| 382.95 |
0.12800 |
0.59500 |
| 379.95 |
0.14700 |
0.64300 |
| 377.85 |
0.16500 |
0.67000 |
| 376.45 |
0.17500 |
0.69000 |
| 374.05 |
0.20000 |
0.72000 |
| 371.65 |
0.23800 |
0.74500 |
| 368.85 |
0.28100 |
0.78000 |
| 365.25 |
0.37500 |
0.81800 |
| 361.85 |
0.49800 |
0.85500 |
| 359.85 |
0.60700 |
0.88000 |
| 358.65 |
0.69400 |
0.89700 |
| 357.25 |
0.78700 |
0.91800 |
| 356.25 |
0.87200 |
0.94000 |
| 354.95 |
0.95700 |
0.97400 |
| 354.75 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Di Cave S.; Mazzarotta B.: Isobaric Vapor-Liquid Equilibria for the Binary Systems Formed by Acetonitrile and Aromatic Hydrocarbons. J.Chem.Eng.Data 36 (1991) 293-297 |
Diagrams
List of All References
| Source |
| Bagga O.P.; Katyal R.C.; Raju K.S.N.: Acetonitrile-Ethylbenzene and Acetonitrile-p-Xylene. J.Chem.Eng.Data 22 (1977) 416-418 |
| Di Cave S.; Mazzarotta B.: Isobaric Vapor-Liquid Equilibria for the Binary Systems Formed by Acetonitrile and Aromatic Hydrocarbons. J.Chem.Eng.Data 36 (1991) 293-297 |
Vapor-Liquid Equilibrium Data Overview
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