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 536

Components

No. Formula Molar Mass CAS Registry Number Name
1 C2H6O 46.069 64-17-5 Ethanol
2 C3H8O 60.096 67-63-0 2-Propanol
Search the DDB for all data of this mixture

Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
355.05 0.12400 0.14100
354.55 0.24000 0.26650
354.45 0.24250 0.27300
354.15 0.34800 0.38450
353.65 0.45550 0.48500
353.65 0.45700 0.49550
353.35 0.55200 0.58950
353.25 0.55900 0.59700
353.05 0.61350 0.64600
352.55 0.74250 0.77000
352.25 0.82950 0.85450
352.25 0.83350 0.85800
351.95 0.91500 0.92950

(T - temperature, x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Ballard L.H.; van Winkle M.: Vapor-Liquid Equilibria at 760 Mm. Pressure. 2-Propanol-Methanol, 2-Propanol-Ethyl Alcohol, 2-Propanol-Propanol, and 2-Propanol-2-Butyl Alcohol Systems. Ind.Eng.Chem. 44 (1952) 2450-2453


Vapor-Liquid Equilibrium Data Set 2850

Components

No. Formula Molar Mass CAS Registry Number Name
1 C2H6O 46.069 64-17-5 Ethanol
2 C3H8O 60.096 67-63-0 2-Propanol
Search the DDB for all data of this mixture

Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol] y1 [mol/mol]
355.54 0.00000 0.00000
354.65 0.18000 0.19350
354.30 0.30200 0.32350
354.03 0.36550 0.41400
353.83 0.40100 0.42750
353.42 0.51400 0.56000
353.25 0.54100 0.57250
353.05 0.62900 0.66200
352.72 0.71820 0.75360
352.18 0.79160 0.82500
352.10 0.86060 0.87050
351.61 1.00000 1.00000

(T - temperature, x - liquid mole fraction, y - vapor mole fraction)

Reference

Source
Kojima K.; Ochi K.; Nakazawa Y.: Relationship between Liquid Activity Coefficient and Composition for Ternary Systems. Int.Chem.Eng. 9 (1969) 342-347

Diagrams

Vapor-Liquid Equilibrium of Ethanol+2-Propanol
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Vapor-Liquid Equilibrium of Ethanol+2-Propanol
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List of All References

Source
Ballard L.H.; van Winkle M.: Vapor-Liquid Equilibria at 760 Mm. Pressure. 2-Propanol-Methanol, 2-Propanol-Ethyl Alcohol, 2-Propanol-Propanol, and 2-Propanol-2-Butyl Alcohol Systems. Ind.Eng.Chem. 44 (1952) 2450-2453
Kojima K.; Ochi K.; Nakazawa Y.: Relationship between Liquid Activity Coefficient and Composition for Ternary Systems. Int.Chem.Eng. 9 (1969) 342-347

Vapor-Liquid Equilibrium Data Overview


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