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 416
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 350.65 |
0.07100 |
0.06400 |
| 350.75 |
0.11000 |
0.10200 |
| 350.85 |
0.14000 |
0.13400 |
| 350.95 |
0.17400 |
0.17100 |
| 350.95 |
0.22300 |
0.22700 |
| 350.65 |
0.25900 |
0.27000 |
| 350.45 |
0.30100 |
0.32300 |
| 349.95 |
0.36500 |
0.40800 |
| 349.15 |
0.44800 |
0.52200 |
| 348.25 |
0.50400 |
0.59600 |
| 347.85 |
0.52800 |
0.62800 |
| 346.65 |
0.58100 |
0.70000 |
| 344.95 |
0.65000 |
0.78000 |
| 343.55 |
0.70400 |
0.83900 |
| 342.05 |
0.75100 |
0.87900 |
| 340.85 |
0.79000 |
0.91000 |
| 338.75 |
0.85600 |
0.95000 |
| 336.85 |
0.92200 |
0.97800 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Nagata I.: Isobaric Vapor-Liquid Equilibria for the Ternary System Chloroform-Methanol-Ethyl Acetate. J.Chem.Eng.Data 7 (1962) 367-373 |
Vapor-Liquid Equilibrium Data Set 2139
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
| 350.25 |
0.00000 |
| 350.50 |
0.08020 |
| 350.60 |
0.14720 |
| 350.70 |
0.19790 |
| 350.60 |
0.23310 |
| 350.50 |
0.26770 |
| 350.30 |
0.30560 |
| 349.50 |
0.39300 |
| 349.00 |
0.43780 |
| 348.80 |
0.46150 |
| 347.75 |
0.54610 |
| 347.15 |
0.59220 |
| 346.45 |
0.63230 |
| 345.25 |
0.67760 |
| 344.90 |
0.70220 |
| 343.25 |
0.74170 |
| 341.35 |
0.79550 |
| 339.85 |
0.83610 |
| 337.35 |
0.90780 |
| 336.15 |
0.94380 |
| 334.35 |
1.00000 |
(T - temperature, x - liquid mole fraction)
Reference
| Source |
| Fahmy A.F.M.; El-Ghannam N.I.M.: The Boiling Temperature-Composition Behaviour in Binary Systems of Alkanol Acetates with Entrainers. Bull.Acad.Pol.Sci.Ser.Sci.Chim. 20 (1972) 101-106 |
Vapor-Liquid Equilibrium Data Set 3255
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 350.35 |
0.04500 |
0.03900 |
| 350.65 |
0.13000 |
0.12000 |
| 350.55 |
0.20100 |
0.21000 |
| 350.45 |
0.27400 |
0.29500 |
| 350.25 |
0.31100 |
0.32700 |
| 350.15 |
0.34900 |
0.38900 |
| 349.75 |
0.36800 |
0.42200 |
| 349.65 |
0.38500 |
0.44000 |
| 349.15 |
0.43800 |
0.51800 |
| 348.35 |
0.50400 |
0.60200 |
| 347.45 |
0.55800 |
0.66500 |
| 346.55 |
0.61100 |
0.71800 |
| 345.35 |
0.65100 |
0.78500 |
| 342.15 |
0.75400 |
0.88200 |
| 339.95 |
0.83100 |
0.93500 |
| 337.65 |
0.89400 |
0.96000 |
| 335.25 |
0.94600 |
0.97900 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Fahmy A.F.M.; El-Ghannam N.I.M.: Vapour-Liquid Equilibrium in the Ethyl Acetate-Chloroform and Methyl Acetate-Carbon Disulphide Mixtures. III. Bull.Acad.Pol.Sci.Ser.Sci.Chim. 20 (1972) 493-497 |
Diagrams
List of All References
| Source |
| Nagata I.: Isobaric Vapor-Liquid Equilibria for the Ternary System Chloroform-Methanol-Ethyl Acetate. J.Chem.Eng.Data 7 (1962) 367-373 |
| Fahmy A.F.M.; El-Ghannam N.I.M.: Vapour-Liquid Equilibrium in the Ethyl Acetate-Chloroform and Methyl Acetate-Carbon Disulphide Mixtures. III. Bull.Acad.Pol.Sci.Ser.Sci.Chim. 20 (1972) 493-497 |
| Fahmy A.F.M.; El-Ghannam N.I.M.: The Boiling Temperature-Composition Behaviour in Binary Systems of Alkanol Acetates with Entrainers. Bull.Acad.Pol.Sci.Ser.Sci.Chim. 20 (1972) 101-106 |
Vapor-Liquid Equilibrium Data Overview
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