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 1394
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
2 |
C2H6O2 |
62.068 |
107-21-1 |
1,2-Ethanediol |
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Constant Value
Data Table
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
472.15 |
0.00000 |
0.00000 |
461.75 |
0.01000 |
0.15200 |
453.45 |
0.01500 |
0.36800 |
444.25 |
0.02700 |
0.54000 |
439.15 |
0.03200 |
0.61000 |
420.35 |
0.07500 |
0.84500 |
404.65 |
0.10000 |
0.92200 |
383.15 |
0.14200 |
0.96000 |
374.15 |
0.18500 |
0.98500 |
362.35 |
0.25000 |
0.99500 |
350.65 |
0.36000 |
0.99500 |
341.15 |
0.59000 |
0.99800 |
338.65 |
0.75400 |
0.99900 |
337.25 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Baker T.H.; Fisher G.T.; Roth J.A.: Vapor Liquid Equilibrium and Refractive Indices of the Methanol-Ethylene Glycol System. J.Chem.Eng.Data 9 (1964) 11-12 |
Vapor-Liquid Equilibrium Data Set 2620
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
2 |
C2H6O2 |
62.068 |
107-21-1 |
1,2-Ethanediol |
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Constant Value
Data Table
T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
400.95 |
0.19840 |
0.91590 |
375.65 |
0.29790 |
0.96700 |
355.05 |
0.49800 |
0.98800 |
347.25 |
0.69420 |
0.99080 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Chandramouli V.V.; Laddha G.S.: Vapour-Liquid Equilibria: Acetone-Methanol-Ethylene Glycol System. J.Sci.Ind.Res.B:Phys.Sci. 21 (1962) 269-274 |
Vapor-Liquid Equilibrium Data Set 5026
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
2 |
C2H6O2 |
62.068 |
107-21-1 |
1,2-Ethanediol |
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Constant Value
Data Table
P [kPa] |
x1 [mol/mol] |
11.599 |
0.29900 |
16.932 |
0.44700 |
20.532 |
0.55000 |
24.265 |
0.65300 |
29.198 |
0.79300 |
32.931 |
0.91000 |
(P - pressure, x - liquid mole fraction)
Reference
Source |
Sedletskaya I.S.; Kogan V.B.: Investigation of Liquid-Vapor Equilibrium and Tests of Thermodynamic Consistency of experimental Data for a Ternary System with a Nonvolatile Component. J.Appl.Chem.USSR 42 (1969) 2403-2407 |
Diagrams
List of All References
Source |
Baker T.H.; Fisher G.T.; Roth J.A.: Vapor Liquid Equilibrium and Refractive Indices of the Methanol-Ethylene Glycol System. J.Chem.Eng.Data 9 (1964) 11-12 |
Chandramouli V.V.; Laddha G.S.: Vapour-Liquid Equilibria: Acetone-Methanol-Ethylene Glycol System. J.Sci.Ind.Res.B:Phys.Sci. 21 (1962) 269-274 |
Sedletskaya I.S.; Kogan V.B.: Investigation of Liquid-Vapor Equilibrium and Tests of Thermodynamic Consistency of experimental Data for a Ternary System with a Nonvolatile Component. J.Appl.Chem.USSR 42 (1969) 2403-2407 |
Vapor-Liquid Equilibrium Data Overview
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