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 3560

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O2 88.106 141-78-6 Ethyl acetate
2 H2O 18.015 7732-18-5 Water
3 C6H6 78.114 71-43-2 Benzene
4 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] x2 [mol/mol] x3 [mol/mol] y1 [mol/mol] y2 [mol/mol] y3 [mol/mol]
347.58 0.20000 0.64000 0.06400 0.43900 0.40100 0.13100
345.55 0.40000 0.48000 0.04800 0.53800 0.37000 0.07600
344.68 0.60000 0.32000 0.03200 0.61900 0.33300 0.03900
344.81 0.80000 0.16000 0.01600 0.66000 0.32200 0.01400
349.22 0.20000 0.48000 0.12800 0.32000 0.42700 0.20300
346.79 0.40000 0.36000 0.09600 0.48800 0.34600 0.13800
345.76 0.60000 0.24000 0.06400 0.58100 0.33400 0.07000
345.89 0.80000 0.12000 0.03200 0.67800 0.28400 0.03000
350.24 0.20000 0.32000 0.19200 0.27900 0.40100 0.25600
347.70 0.40000 0.24000 0.14400 0.41000 0.38700 0.16600
346.57 0.60000 0.16000 0.09600 0.52700 0.35500 0.09800
347.56 0.80000 0.08000 0.04800 0.68600 0.26600 0.03800
351.19 0.20000 0.16000 0.25600 0.22900 0.44900 0.27300
350.33 0.40000 0.12000 0.19200 0.37500 0.39700 0.18600
349.37 0.60000 0.08000 0.12800 0.55100 0.30000 0.12000
349.90 0.80000 0.04000 0.06400 0.74800 0.17700 0.05900
348.35 0.20000 0.64000 0.03200 0.46000 0.39900 0.08500
345.65 0.40000 0.48000 0.02400 0.54500 0.39200 0.03900
344.25 0.60000 0.32000 0.01600 0.62200 0.34200 0.02500
344.15 0.80000 0.16000 0.00800 0.67900 0.30500 0.01100
350.15 0.20000 0.48000 0.06400 0.39400 0.41000 0.10900
347.65 0.40000 0.36000 0.04800 0.52000 0.38000 0.06500
345.55 0.60000 0.24000 0.03200 0.59500 0.35000 0.04000
345.75 0.80000 0.12000 0.01600 0.70300 0.26900 0.02000
351.75 0.20000 0.32000 0.09600 0.30600 0.42400 0.16400
349.05 0.40000 0.24000 0.07200 0.45900 0.38600 0.09100
347.15 0.60000 0.16000 0.04800 0.56700 0.34600 0.05400
346.95 0.80000 0.08000 0.02400 0.73500 0.22900 0.02500
353.45 0.20000 0.16000 0.12800 0.26800 0.44900 0.16300
351.05 0.40000 0.12000 0.09600 0.48700 0.31600 0.12000
349.85 0.60000 0.08000 0.06400 0.63000 0.25900 0.06700
348.75 0.80000 0.04000 0.03200 0.77800 0.17000 0.03700
345.25 0.20000 0.64000 0.09600 0.43300 0.32100 0.22800
344.25 0.40000 0.48000 0.07200 0.57200 0.29500 0.12300
343.75 0.60000 0.32000 0.04800 0.63700 0.30400 0.05400
344.15 0.80000 0.16000 0.02400 0.68300 0.29200 0.02200
346.35 0.20000 0.48000 0.19200 0.33500 0.31000 0.33600
345.25 0.40000 0.36000 0.14400 0.47900 0.30800 0.19700
344.15 0.60000 0.24000 0.09600 0.58900 0.29000 0.11000
345.05 0.80000 0.12000 0.04800 0.69800 0.25300 0.04500
347.15 0.20000 0.32000 0.28800 0.26000 0.30300 0.39000
345.45 0.40000 0.24000 0.21600 0.41800 0.29500 0.26000
345.15 0.60000 0.16000 0.14400 0.54200 0.30100 0.14100
345.95 0.80000 0.08000 0.07200 0.71000 0.21700 0.06700
347.55 0.20000 0.16000 0.38400 0.22400 0.31300 0.42600
346.35 0.40000 0.12000 0.28800 0.38000 0.31600 0.27600
345.95 0.60000 0.08000 0.19200 0.55400 0.25100 0.17800
348.35 0.80000 0.04000 0.09600 0.73500 0.18000 0.07900

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

Reference

Source
Anton N.D.; Babich S.V.; Tikhonova N.K.; Timofeev V.S.; Serafimov L.A.: Liquid-Vapor Equilibria in the System Ethyl Acetate-Benzene-Water-Butyl Acetate. J.Appl.Chem.USSR 49 (1976) 341-344


Vapor-Liquid Equilibrium Data Set 27358

Components

No. Formula Molar Mass CAS Registry Number Name
1 C4H8O2 88.106 141-78-6 Ethyl acetate
2 H2O 18.015 7732-18-5 Water
3 C6H6 78.114 71-43-2 Benzene
4 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] x2 [mol/mol] x3 [mol/mol] y1 [mol/mol] y2 [mol/mol] y3 [mol/mol]
0.64000 0.20000 0.12800 0.29700 0.40300 0.28900
0.48000 0.40000 0.09600 0.29300 0.54100 0.16100
0.31800 0.60200 0.06400 0.34200 0.58100 0.07500
0.16000 0.80000 0.03200 0.33400 0.63400 0.03100
0.48200 0.19800 0.25600 0.29600 0.29200 0.39700
0.32800 0.36300 0.24700 0.28700 0.40300 0.30000
0.23800 0.60000 0.12800 0.33500 0.52900 0.13200
0.80000 0.12000 0.06400 0.28100 0.65800 0.05900
0.32000 0.20000 0.38400 0.34900 0.22400 0.41100
0.24000 0.40000 0.28800 0.30000 0.39400 0.29400
0.15800 0.60200 0.19200 0.30000 0.51100 0.18300
0.08000 0.80000 0.09600 0.28400 0.62100 0.09200
0.20000 0.25000 0.44000 0.30500 0.24300 0.43600
0.12000 0.40000 0.38400 0.35100 0.32400 0.31200
0.08000 0.60000 0.25600 0.27400 0.51400 0.20200
0.04000 0.80000 0.12300 0.12300 0.75800 0.11400

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

Reference

Source
Anton N.D.; Babich S.V.; Tikhonova N.K.; Timofeev V.S.; Serafimov L.A.: Liquid-Vapor Equilibria in the System Ethyl Acetate-Benzene-Water-Butyl Acetate. J.Appl.Chem.USSR 49 (1976) 341-344


Vapor-Liquid Equilibrium Data Set 27359

Components

No. Formula Molar Mass CAS Registry Number Name
1 H2O 18.015 7732-18-5 Water
2 C4H8O2 88.106 141-78-6 Ethyl acetate
3 C6H6 78.114 71-43-2 Benzene
4 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] x2 [mol/mol] x3 [mol/mol]
344.75 0.30000 0.15000 0.44000
343.85 0.30000 0.35000 0.28000
343.45 0.29800 0.55100 0.12100
344.45 0.60000 0.30000 0.08000
343.45 0.60000 0.10000 0.24000
343.75 0.60000 0.20000 0.16000
348.15 0.01000 0.84800 0.10400
345.85 0.10000 0.77000 0.01400
344.65 0.14900 0.72900 0.09800

(T - temperature, x - liquid mole fraction)

Reference

Source
Anton N.D.; Babich S.V.; Tikhonova N.K.; Timofeev V.S.; Serafimov L.A.: Liquid-Vapor Equilibria in the System Ethyl Acetate-Benzene-Water-Butyl Acetate. J.Appl.Chem.USSR 49 (1976) 341-344

List of All References

Source

Vapor-Liquid Equilibrium Data Overview


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