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 1828

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O 72.107 109-99-9 Tetrahydrofuran
2 C4H10O 74.123 71-36-3 1-Butanol
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]
380.30 0.10000 0.38950
372.00 0.20000 0.60110
365.30 0.30000 0.73710
359.70 0.40000 0.82150
355.15 0.50000 0.87850
351.15 0.60000 0.91870
347.50 0.70000 0.94860
344.45 0.80000 0.96980
341.45 0.90000 0.98680

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

Reference

Source
Shnitko V.A.; Kogan V.B.; Petrova N.V.: Tetrahydrofuran - Butanol-1. Zh.Prikl.Khim. 44 (1971) 2126-2128


Vapor-Liquid Equilibrium Data Set 15877

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O 72.107 109-99-9 Tetrahydrofuran
2 C4H10O 74.123 71-36-3 1-Butanol
Search the DDB for all data of this mixture

Constant Value

Pressure 101.33 kPa

Data Table

T [K] x1 [mol/mol]
383.15 0.05000
378.55 0.10000
373.95 0.15000
371.15 0.20000
368.35 0.25000
366.15 0.30000
363.75 0.35000
361.75 0.40000
359.35 0.45000
357.05 0.50000
354.75 0.55000
352.35 0.60000
349.95 0.65000
348.15 0.70000
346.35 0.75000
344.75 0.80000
343.15 0.85000
341.75 0.90000
340.35 0.95000

(T - temperature, x - liquid mole fraction)

Reference

Source
Khrennikova O.V.; Egorenko G.A.; Samsonova N.I.; Semenova L.V.; Rodina G.L.: Untersuchung des Dampf-Flüssig-Gleichgewichtes in binären Systemen Tetrahydrofuran-Beimischung. Chimiceskie reaktivy i osobo cistye vescestva 52 (1990) 51-58


Vapor-Liquid Equilibrium Data Set 27139

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O 72.107 109-99-9 Tetrahydrofuran
2 C4H10O 74.123 71-36-3 1-Butanol
Search the DDB for all data of this mixture

Constant Value

Pressure 95.80 kPa

Data Table

T [K] x1 [mol/mol]
389.45 0.00000
370.65 0.13380
360.45 0.24360
354.75 0.32570
350.95 0.39180
348.25 0.44600
346.35 0.49140
342.15 0.61230
340.75 0.66370
339.35 0.72470
337.95 0.82060
337.25 0.88760
337.55 1.00000

(T - temperature, x - liquid mole fraction)

Reference

Source
Vittal Prasad T.E.; Raj E.D.A.; Maheedhar G.; Reddy M.S.; Kumar V.S.; Garapati S.; Patanjali V.; Prasad D.H.L.: Bubble-Temperature Measurements on Some Binary Mixtures formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa. J.Chem.Eng.Data 49 (2004) 746-749

Diagrams

Vapor-Liquid Equilibrium of 1-Butanol+Tetrahydrofuran
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Vapor-Liquid Equilibrium of 1-Butanol+Tetrahydrofuran
See larger image

List of All References

Source
Shnitko V.A.; Kogan V.B.; Petrova N.V.: Tetrahydrofuran - Butanol-1. Zh.Prikl.Khim. 44 (1971) 2126-2128
Khrennikova O.V.; Egorenko G.A.; Samsonova N.I.; Semenova L.V.; Rodina G.L.: Untersuchung des Dampf-Flüssig-Gleichgewichtes in binären Systemen Tetrahydrofuran-Beimischung. Chimiceskie reaktivy i osobo cistye vescestva 52 (1990) 51-58
Vittal Prasad T.E.; Raj E.D.A.; Maheedhar G.; Reddy M.S.; Kumar V.S.; Garapati S.; Patanjali V.; Prasad D.H.L.: Bubble-Temperature Measurements on Some Binary Mixtures formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa. J.Chem.Eng.Data 49 (2004) 746-749

Vapor-Liquid Equilibrium Data Overview


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