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 14177
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 2 |
C8H10 |
106.167 |
108-38-3 |
m-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 369.95 |
0.00000 |
0.00000 |
| 366.35 |
0.01100 |
0.12300 |
| 364.85 |
0.01300 |
0.15700 |
| 363.85 |
0.01700 |
0.19500 |
| 360.55 |
0.02700 |
0.28000 |
| 357.55 |
0.03400 |
0.35800 |
| 354.55 |
0.04300 |
0.43000 |
| 353.65 |
0.04600 |
0.44500 |
| 351.75 |
0.05400 |
0.49000 |
| 348.55 |
0.06300 |
0.54800 |
| 341.35 |
0.10500 |
0.67300 |
| 339.95 |
0.12700 |
0.69800 |
| 338.75 |
0.14200 |
0.71500 |
| 336.55 |
0.16200 |
0.74800 |
| 335.25 |
0.18500 |
0.76100 |
| 332.95 |
0.22100 |
0.79100 |
| 330.75 |
0.26300 |
0.81900 |
| 328.55 |
0.31700 |
0.85100 |
| 326.95 |
0.38200 |
0.86800 |
| 325.95 |
0.44500 |
0.88100 |
| 324.75 |
0.52500 |
0.88600 |
| 323.75 |
0.58500 |
0.90100 |
| 323.55 |
0.60000 |
0.90700 |
| 322.05 |
0.68700 |
0.92200 |
| 321.25 |
0.77800 |
0.93500 |
| 320.25 |
0.86500 |
0.95300 |
| 319.95 |
0.92500 |
0.96700 |
| 319.65 |
0.96200 |
0.97900 |
| 319.05 |
0.99400 |
0.99600 |
| 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 14178
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 2 |
C8H10 |
106.167 |
108-38-3 |
m-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 412.15 |
0.00000 |
0.00000 |
| 410.65 |
0.00800 |
0.05200 |
| 408.85 |
0.01500 |
0.09800 |
| 407.25 |
0.02000 |
0.12500 |
| 405.75 |
0.02200 |
0.14800 |
| 404.25 |
0.03000 |
0.19200 |
| 403.25 |
0.03500 |
0.21500 |
| 402.55 |
0.03800 |
0.23800 |
| 401.55 |
0.04000 |
0.25800 |
| 400.35 |
0.04800 |
0.29000 |
| 399.15 |
0.05100 |
0.30500 |
| 397.55 |
0.05600 |
0.33800 |
| 396.15 |
0.06200 |
0.36800 |
| 394.75 |
0.06500 |
0.39200 |
| 392.65 |
0.07800 |
0.43800 |
| 390.65 |
0.08000 |
0.47200 |
| 389.15 |
0.08700 |
0.49700 |
| 386.55 |
0.10000 |
0.54300 |
| 381.85 |
0.13100 |
0.61500 |
| 380.35 |
0.14500 |
0.64500 |
| 378.35 |
0.16000 |
0.68200 |
| 375.95 |
0.18700 |
0.70700 |
| 373.55 |
0.21800 |
0.73000 |
| 373.25 |
0.22700 |
0.73500 |
| 371.05 |
0.25000 |
0.76300 |
| 367.25 |
0.33000 |
0.79500 |
| 367.05 |
0.33200 |
0.80500 |
| 365.05 |
0.39000 |
0.82700 |
| 364.45 |
0.39700 |
0.83000 |
| 363.35 |
0.43400 |
0.84000 |
| 363.05 |
0.44500 |
0.84700 |
| 361.95 |
0.46500 |
0.85300 |
| 361.85 |
0.48000 |
0.85800 |
| 360.05 |
0.58300 |
0.87800 |
| 359.45 |
0.63500 |
0.88800 |
| 358.35 |
0.72300 |
0.90500 |
| 357.65 |
0.76600 |
0.91500 |
| 357.25 |
0.81000 |
0.92500 |
| 356.65 |
0.85000 |
0.93500 |
| 356.05 |
0.88800 |
0.94800 |
| 355.65 |
0.93000 |
0.96200 |
| 355.45 |
0.95800 |
0.97200 |
| 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 |
| 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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