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 1800
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 365.35 |
0.00250 |
0.01680 |
0.06360 |
0.19600 |
| 357.95 |
0.00430 |
0.05070 |
0.08050 |
0.39550 |
| 351.85 |
0.00840 |
0.10500 |
0.07510 |
0.48200 |
| 357.15 |
0.01360 |
0.02410 |
0.23300 |
0.19700 |
| 349.95 |
0.01370 |
0.19600 |
0.07550 |
0.54400 |
| 349.75 |
0.01920 |
0.28600 |
0.07560 |
0.56200 |
| 349.95 |
0.01980 |
0.68100 |
0.03540 |
0.66800 |
| 353.15 |
0.02000 |
0.02840 |
0.31400 |
0.20100 |
| 349.35 |
0.02580 |
0.41900 |
0.07040 |
0.57000 |
| 348.55 |
0.03640 |
0.66100 |
0.07210 |
0.63600 |
| 350.75 |
0.04290 |
0.88340 |
0.08010 |
0.79100 |
| 346.35 |
0.06080 |
0.05820 |
0.44500 |
0.21900 |
| 347.35 |
0.08100 |
0.64200 |
0.14300 |
0.57500 |
| 348.15 |
0.08900 |
0.74300 |
0.15600 |
0.61300 |
| 348.65 |
0.09610 |
0.81900 |
0.17200 |
0.68500 |
| 346.15 |
0.11100 |
0.61100 |
0.18700 |
0.54200 |
| 346.15 |
0.13900 |
0.72700 |
0.23800 |
0.58800 |
| 341.05 |
0.14400 |
0.04550 |
0.62800 |
0.10600 |
| 339.15 |
0.16200 |
0.05400 |
0.62400 |
0.10480 |
| 341.55 |
0.18300 |
0.14100 |
0.51700 |
0.20900 |
| 344.35 |
0.19600 |
0.54200 |
0.31600 |
0.43300 |
| 344.35 |
0.20000 |
0.64000 |
0.33400 |
0.49200 |
| 341.75 |
0.26800 |
0.50100 |
0.41700 |
0.36800 |
| 342.75 |
0.28600 |
0.56400 |
0.43600 |
0.40700 |
| 338.55 |
0.32100 |
0.18700 |
0.60700 |
0.17400 |
| 340.75 |
0.33800 |
0.45200 |
0.50000 |
0.32100 |
| 340.65 |
0.34200 |
0.46900 |
0.50800 |
0.32900 |
| 336.35 |
0.35800 |
0.09180 |
0.71100 |
0.08900 |
| 338.15 |
0.44800 |
0.34200 |
0.61500 |
0.22600 |
| 337.45 |
0.49000 |
0.26400 |
0.66600 |
0.17500 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Pratt H.R.C.: Continuous Purification and Azeotropic Dehydration of Acetonitrile Produced by the Catalytic Acetic Acid-Ammonia Reaction. Trans.Inst.Chem.Engr. 25 (1947) 43-67 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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