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 2003
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 2 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 384.15 |
0.04600 |
0.22210 |
| 380.75 |
0.08150 |
0.34280 |
| 378.65 |
0.10500 |
0.40740 |
| 373.75 |
0.16950 |
0.54000 |
| 369.70 |
0.23100 |
0.62920 |
| 368.70 |
0.24050 |
0.64100 |
| 366.60 |
0.28400 |
0.68770 |
| 365.15 |
0.31450 |
0.71470 |
| 362.00 |
0.39650 |
0.77620 |
| 360.75 |
0.43100 |
0.79430 |
| 359.15 |
0.49900 |
0.82790 |
| 357.75 |
0.54850 |
0.84870 |
| 356.35 |
0.60200 |
0.87100 |
| 355.15 |
0.65150 |
0.88670 |
| 353.85 |
0.71700 |
0.90760 |
| 352.75 |
0.77350 |
0.92490 |
| 351.70 |
0.82500 |
0.94100 |
| 350.45 |
0.89100 |
0.96030 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Mainkar S.V.; Mene P.S.: Binary Vapor-Liquid Equilibrium Data for Ethyl Acetate-n-Butanol System. Indian J.Technol. 3 (1965) 228-229 |
Vapor-Liquid Equilibrium Data Set 4634
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 2 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
| 390.85 |
0.00000 |
| 383.15 |
0.08550 |
| 377.05 |
0.17380 |
| 371.65 |
0.26500 |
| 367.75 |
0.35930 |
| 363.55 |
0.45690 |
| 360.05 |
0.55790 |
| 357.05 |
0.66250 |
| 354.55 |
0.77090 |
| 352.35 |
0.88330 |
(T - temperature, x - liquid mole fraction)
Reference
| Source |
| Litkenhous E.E.; van Arsdale J.D.; Hutchison I.W.: The Physical Properties of the Ternary System Butyl Alcohol-Ethyl Acetate Toluene. J.Phys.Chem. 44 (1940) 377-388 |
Vapor-Liquid Equilibrium Data Set 10967
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 2 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 384.65 |
0.04930 |
0.27500 |
| 381.15 |
0.08270 |
0.32000 |
| 378.15 |
0.12400 |
0.41700 |
| 376.45 |
0.13100 |
0.45400 |
| 371.05 |
0.23800 |
0.60800 |
| 366.45 |
0.32500 |
0.69500 |
| 362.65 |
0.39400 |
0.75200 |
| 361.15 |
0.45700 |
0.79300 |
| 359.85 |
0.54700 |
0.83500 |
| 358.35 |
0.61300 |
0.85200 |
| 356.65 |
0.68000 |
0.88300 |
| 355.35 |
0.75400 |
0.90600 |
| 354.55 |
0.77900 |
0.91600 |
| 353.25 |
0.84300 |
0.94300 |
| 352.45 |
0.88200 |
0.95800 |
| 351.75 |
0.90600 |
0.96700 |
| 350.25 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Shono H.; Kanazawa N.; Hashitani M.; Komatsu H.; Hirata M.: Vapor-Liquid Equilibrium in Extractive Distillation of Ethyl Acetate-Ethanol System. Kogyo Kagaku Zasshi 72 (1969) 815-819 |
Diagrams
List of All References
| Source |
| Mainkar S.V.; Mene P.S.: Binary Vapor-Liquid Equilibrium Data for Ethyl Acetate-n-Butanol System. Indian J.Technol. 3 (1965) 228-229 |
| Litkenhous E.E.; van Arsdale J.D.; Hutchison I.W.: The Physical Properties of the Ternary System Butyl Alcohol-Ethyl Acetate Toluene. J.Phys.Chem. 44 (1940) 377-388 |
| Shono H.; Kanazawa N.; Hashitani M.; Komatsu H.; Hirata M.: Vapor-Liquid Equilibrium in Extractive Distillation of Ethyl Acetate-Ethanol System. Kogyo Kagaku Zasshi 72 (1969) 815-819 |
Vapor-Liquid Equilibrium Data Overview
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