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 420
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
60-29-7 |
Diethyl ether |
| 2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 9.413 |
0.00000 |
0.00000 |
| 23.465 |
0.09800 |
0.61500 |
| 33.464 |
0.20400 |
0.75000 |
| 42.876 |
0.38000 |
0.83100 |
| 53.996 |
0.75300 |
0.93100 |
| 59.608 |
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 11844
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
60-29-7 |
Diethyl ether |
| 2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 11.838 |
0.00000 |
| 20.705 |
0.04300 |
| 27.220 |
0.08150 |
| 35.070 |
0.14090 |
| 41.721 |
0.20680 |
| 48.469 |
0.30060 |
| 53.430 |
0.39620 |
| 57.490 |
0.49810 |
| 60.700 |
0.59650 |
| 63.660 |
0.69710 |
| 66.111 |
0.78570 |
| 67.870 |
0.85110 |
| 69.540 |
0.91420 |
| 70.450 |
0.95020 |
| 71.499 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Srivastava R.; Natarajan G.; Smith B.D.: Total Pressure Vapor-Liquid Equilibrium Data for Binary Systems of Diethyl Ether with Acetone, Acetonitrile, and Methanol. J.Chem.Eng.Data 31 (1986) 89-93 |
Vapor-Liquid Equilibrium Data Set 11845
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
60-29-7 |
Diethyl ether |
| 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] |
| 58.630 |
0.00000 |
| 87.370 |
0.04280 |
| 109.110 |
0.08140 |
| 135.740 |
0.14040 |
| 158.900 |
0.20060 |
| 183.500 |
0.29970 |
| 201.910 |
0.39490 |
| 217.650 |
0.49720 |
| 230.020 |
0.59550 |
| 241.520 |
0.69640 |
| 250.419 |
0.78510 |
| 256.590 |
0.85080 |
| 262.050 |
0.91400 |
| 264.760 |
0.95010 |
| 267.430 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Srivastava R.; Natarajan G.; Smith B.D.: Total Pressure Vapor-Liquid Equilibrium Data for Binary Systems of Diethyl Ether with Acetone, Acetonitrile, and Methanol. J.Chem.Eng.Data 31 (1986) 89-93 |
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 |
| Srivastava R.; Natarajan G.; Smith B.D.: Total Pressure Vapor-Liquid Equilibrium Data for Binary Systems of Diethyl Ether with Acetone, Acetonitrile, and Methanol. J.Chem.Eng.Data 31 (1986) 89-93 |
Vapor-Liquid Equilibrium Data Overview
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