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 4967

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H6 78.114 71-43-2 Benzene
2 C6H12O2 116.160 123-86-4 Acetic acid butyl ester
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]
395.75 0.04400 0.13800
393.55 0.07800 0.22500
391.55 0.11400 0.29800
388.85 0.15900 0.38400
385.95 0.20600 0.47300
383.85 0.23800 0.52200
378.85 0.33100 0.65300
377.55 0.36100 0.68200
373.45 0.44100 0.76600
369.05 0.53600 0.83300
366.45 0.59800 0.87000
364.15 0.65500 0.89200
362.25 0.70400 0.91500
360.35 0.75700 0.93400
357.75 0.83500 0.95900
356.65 0.88000 0.97100
355.75 0.91100 0.98000

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

Reference

Source
Nagata I.: Vapor-Liquid Equilibrium Data for Binary Systems, Acetone-Methyl Acetate, Methyl Acetate-Carbon Tetrachloride, Benzene- Butyl Acetate and Cyclohexane-Butyl Actate. Mem.Fac.Technol.Kanazawa Univ. 3 (1964) 197-205


Vapor-Liquid Equilibrium Data Set 6848

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H6 78.114 71-43-2 Benzene
2 C6H12O2 116.160 123-86-4 Acetic acid butyl ester
Search the DDB for all data of this mixture

Constant Value

Pressure 101.33 kPa

Data Table

x1 [mol/mol] y1 [mol/mol]
0.06570 0.17750
0.13850 0.31570
0.17350 0.37300
0.22350 0.42840
0.31950 0.57250
0.44700 0.70300
0.52150 0.76950
0.64750 0.85750
0.76070 0.91460
0.83450 0.95270
0.89300 0.97100
0.93400 0.98400
0.95600 0.98800

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

Reference

Source
Bushmakin I.N.; Baldangiin B.; Molodenko P.Ya.: Liquid-Vapor Equilibrium in the Systems Benzene Butyl Acetate and Carbon Tetrachloride Butyl Acetate. J.Appl.Chem.USSR 38 (1965) 1392-1394


Vapor-Liquid Equilibrium Data Set 8099

Components

No. Formula Molar Mass CAS Registry Number Name
1 C6H6 78.114 71-43-2 Benzene
2 C6H12O2 116.160 123-86-4 Acetic acid butyl ester
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]
399.25 0.00000 0.00000
395.15 0.05000 0.16500
391.75 0.10000 0.30000
385.95 0.20000 0.50300
380.65 0.30000 0.64300
375.75 0.40000 0.74300
370.95 0.50000 0.81700
366.65 0.60000 0.87700
362.95 0.70000 0.92300
359.35 0.80000 0.95800
356.15 0.90000 0.98200
354.65 0.95000 0.99000
353.25 1.00000 1.00000

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

Reference

Source
Anton N.D.; Zheleznova N.I.; Tikhonova N.K.; Timofeev V.S.; Serafimov L.A.: Untersuchung physikalisch-chemischer Eigenschaften im System Benzol-Butylacetat-Wasser. Tr.Mosk.Inst.Tonkoj Khim.Tekhnol. 3 (1973) 115-120

Diagrams

Vapor-Liquid Equilibrium of Benzene+Acetic acid butyl ester
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Vapor-Liquid Equilibrium of Benzene+Acetic acid butyl ester
See larger image

List of All References

Source
Nagata I.: Vapor-Liquid Equilibrium Data for Binary Systems, Acetone-Methyl Acetate, Methyl Acetate-Carbon Tetrachloride, Benzene- Butyl Acetate and Cyclohexane-Butyl Actate. Mem.Fac.Technol.Kanazawa Univ. 3 (1964) 197-205
Bushmakin I.N.; Baldangiin B.; Molodenko P.Ya.: Liquid-Vapor Equilibrium in the Systems Benzene Butyl Acetate and Carbon Tetrachloride Butyl Acetate. J.Appl.Chem.USSR 38 (1965) 1392-1394
Anton N.D.; Zheleznova N.I.; Tikhonova N.K.; Timofeev V.S.; Serafimov L.A.: Untersuchung physikalisch-chemischer Eigenschaften im System Benzol-Butylacetat-Wasser. Tr.Mosk.Inst.Tonkoj Khim.Tekhnol. 3 (1973) 115-120

Vapor-Liquid Equilibrium Data Overview


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