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 1389
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
14.745 |
0.00000 |
0.00000 |
19.598 |
0.15000 |
0.34000 |
21.598 |
0.26000 |
0.45100 |
22.078 |
0.28700 |
0.46000 |
23.331 |
0.40000 |
0.50900 |
24.305 |
0.61800 |
0.64000 |
24.531 |
0.63700 |
0.65200 |
23.971 |
0.80000 |
0.77000 |
23.198 |
0.88000 |
0.83900 |
21.358 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Joukovsky N.I.: XI. Contribution à l'étude des propriétés thermodynamiques des solutions concentrées de composés organiques azotés de la série grasse. Bull.Soc.Chim.Belg. 43 (1934) 397-446 |
Vapor-Liquid Equilibrium Data Set 5058
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
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Constant Value
Data Table
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
323.79 |
0.02840 |
0.10950 |
322.14 |
0.05630 |
0.18160 |
319.33 |
0.11060 |
0.30240 |
318.31 |
0.14470 |
0.34970 |
316.13 |
0.23100 |
0.44490 |
315.41 |
0.26830 |
0.47740 |
314.78 |
0.32400 |
0.51111 |
314.19 |
0.37540 |
0.54190 |
313.84 |
0.40320 |
0.55660 |
313.45 |
0.47360 |
0.59700 |
313.13 |
0.52650 |
0.62300 |
313.11 |
0.54500 |
0.63150 |
312.89 |
0.60580 |
0.65680 |
312.77 |
0.65410 |
0.68290 |
312.75 |
0.68810 |
0.70350 |
312.75 |
0.76540 |
0.74790 |
312.80 |
0.79980 |
0.77340 |
313.16 |
0.87900 |
0.83930 |
313.39 |
0.91250 |
0.87110 |
314.13 |
0.97190 |
0.95360 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Dohnal V.; Holub R.; Pick J.: Vapor-Liquid Equilibrium in the Methanol-Acetonitrile System. Collect.Czech.Chem.Commun. 42 (1977) 1445-1452 |
Vapor-Liquid Equilibrium Data Set 5059
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
Search the DDB for all data of this mixture
Constant Value
Data Table
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
334.40 |
0.03610 |
0.12980 |
330.37 |
0.11100 |
0.28920 |
329.27 |
0.13550 |
0.32950 |
327.77 |
0.17910 |
0.39260 |
325.91 |
0.25950 |
0.46220 |
325.29 |
0.29020 |
0.49440 |
324.67 |
0.33150 |
0.52380 |
324.15 |
0.37380 |
0.54700 |
323.91 |
0.39600 |
0.55510 |
323.22 |
0.47260 |
0.60480 |
323.04 |
0.50740 |
0.62530 |
322.64 |
0.57120 |
0.65780 |
322.44 |
0.63830 |
0.68820 |
322.27 |
0.68700 |
0.71570 |
322.22 |
0.75420 |
0.75440 |
322.27 |
0.81610 |
0.79700 |
322.33 |
0.84710 |
0.82440 |
322.55 |
0.89350 |
0.86230 |
322.80 |
0.92540 |
0.90050 |
323.20 |
0.96530 |
0.94810 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Dohnal V.; Holub R.; Pick J.: Vapor-Liquid Equilibrium in the Methanol-Acetonitrile System. Collect.Czech.Chem.Commun. 42 (1977) 1445-1452 |
Diagrams
List of All References
Source |
Joukovsky N.I.: XI. Contribution à l'étude des propriétés thermodynamiques des solutions concentrées de composés organiques azotés de la série grasse. Bull.Soc.Chim.Belg. 43 (1934) 397-446 |
Dohnal V.; Holub R.; Pick J.: Vapor-Liquid Equilibrium in the Methanol-Acetonitrile System. Collect.Czech.Chem.Commun. 42 (1977) 1445-1452 |
Vapor-Liquid Equilibrium Data Overview
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