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 27361

Components

No. Formula Molar Mass CAS Registry Number Name
1 CH4O 32.042 67-56-1 Methanol
2 C4H8O 72.107 109-99-9 Tetrahydrofuran
3 C2H6O2 62.068 107-21-1 1,2-Ethanediol
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Constant Value

Temperature 313.15 K

Data Table

P [kPa] x1 [mol/mol] x2 [mol/mol] y1 [mol/mol] y2 [mol/mol]
36.530 0.73100 0.13450 0.69900 0.30100
32.797 0.62000 0.11400 0.69800 0.30200
25.865 0.45800 0.08400 0.65400 0.34600
41.597 0.62000 0.26600 0.55100 0.44900
36.530 0.53800 0.23100 0.51200 0.48800
31.197 0.41200 0.17600 0.47700 0.52300
22.665 0.26600 0.11400 0.44800 0.55200
43.063 0.45800 0.45800 0.43100 0.56900
40.130 0.41200 0.41200 0.39700 0.60300
35.997 0.33300 0.33400 0.32650 0.67350
30.131 0.23100 0.23100 0.27100 0.72900
20.665 0.13450 0.13450 0.22400 0.77600
41.597 0.26600 0.62000 0.28100 0.71900
38.397 0.23100 0.53800 0.22800 0.77200
34.530 0.17600 0.41200 0.17600 0.82400
29.198 0.11400 0.26600 0.13000 0.87000
39.597 0.13450 0.73100 0.16300 0.83700
36.664 0.11400 0.62000 0.12300 0.87700
33.731 0.08400 0.45800 0.08900 0.91100

(P - pressure, x - liquid mole fraction, y - vapor 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

List of All References

Source

Vapor-Liquid Equilibrium Data Overview


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