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 1805
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 3 |
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] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 345.15 |
0.07500 |
0.07700 |
0.05700 |
0.23800 |
| 338.55 |
0.08200 |
0.24600 |
0.06000 |
0.47000 |
| 337.25 |
0.14700 |
0.30300 |
0.11800 |
0.49400 |
| 335.05 |
0.12200 |
0.53900 |
0.12200 |
0.61800 |
| 335.95 |
0.12300 |
0.44500 |
0.10800 |
0.57400 |
| 336.95 |
0.07900 |
0.34700 |
0.05900 |
0.51300 |
| 336.25 |
0.06000 |
0.47000 |
0.05000 |
0.58500 |
| 335.25 |
0.05800 |
0.63400 |
0.06400 |
0.66700 |
| 335.45 |
0.04800 |
0.56900 |
0.04500 |
0.64000 |
| 335.35 |
0.04600 |
0.65100 |
0.05100 |
0.68100 |
| 335.55 |
0.04000 |
0.86100 |
0.07600 |
0.81400 |
| 334.55 |
0.10400 |
0.64500 |
0.12600 |
0.66500 |
| 334.55 |
0.10100 |
0.65700 |
0.11800 |
0.67300 |
| 335.15 |
0.06300 |
0.72500 |
0.08300 |
0.71300 |
| 334.45 |
0.08600 |
0.73800 |
0.11800 |
0.71800 |
| 335.15 |
0.08700 |
0.57500 |
0.08700 |
0.64400 |
| 335.25 |
0.07000 |
0.79200 |
0.11100 |
0.75000 |
| 337.65 |
0.25000 |
0.24100 |
0.21800 |
0.44200 |
| 335.95 |
0.21900 |
0.36000 |
0.19700 |
0.54800 |
| 335.65 |
0.19000 |
0.43200 |
0.18000 |
0.58000 |
| 334.25 |
0.13600 |
0.67800 |
0.17800 |
0.66300 |
| 334.45 |
0.12000 |
0.63700 |
0.14400 |
0.65500 |
| 342.15 |
0.31400 |
0.12200 |
0.28100 |
0.31600 |
| 335.55 |
0.22200 |
0.38300 |
0.20400 |
0.54400 |
| 333.65 |
0.20200 |
0.59700 |
0.24200 |
0.61900 |
| 333.45 |
0.18000 |
0.65100 |
0.24000 |
0.63900 |
| 334.25 |
0.09700 |
0.82200 |
0.17800 |
0.74800 |
| 342.95 |
0.41600 |
0.07100 |
0.40900 |
0.23500 |
| 336.75 |
0.36400 |
0.20700 |
0.32900 |
0.41400 |
| 333.15 |
0.28900 |
0.48200 |
0.32200 |
0.55300 |
| 335.15 |
0.34700 |
0.30000 |
0.32900 |
0.48900 |
| 332.15 |
0.22300 |
0.65900 |
0.31900 |
0.60300 |
| 334.05 |
0.38400 |
0.31400 |
0.37600 |
0.47500 |
| 332.15 |
0.34500 |
0.46500 |
0.38800 |
0.52600 |
| 331.45 |
0.33800 |
0.50400 |
0.39800 |
0.53100 |
| 330.45 |
0.32700 |
0.57900 |
0.43300 |
0.50900 |
| 330.65 |
0.26500 |
0.66000 |
0.40100 |
0.55800 |
| 334.55 |
0.48600 |
0.21100 |
0.46300 |
0.41200 |
| 334.75 |
0.50700 |
0.19100 |
0.48500 |
0.38000 |
| 332.95 |
0.47000 |
0.28500 |
0.46700 |
0.42600 |
| 331.05 |
0.41900 |
0.40700 |
0.47000 |
0.47800 |
| 338.85 |
0.59700 |
0.07700 |
0.60300 |
0.24200 |
| 333.15 |
0.52700 |
0.21900 |
0.50900 |
0.39300 |
| 330.65 |
0.49900 |
0.33800 |
0.51500 |
0.43700 |
| 330.45 |
0.49200 |
0.36300 |
0.51200 |
0.44900 |
| 329.15 |
0.43400 |
0.48600 |
0.52900 |
0.44800 |
| 329.85 |
0.39700 |
0.51800 |
0.48800 |
0.47500 |
| 332.85 |
0.58800 |
0.18300 |
0.57000 |
0.36100 |
| 336.95 |
0.65300 |
0.08200 |
0.65200 |
0.24700 |
| 330.55 |
0.60800 |
0.23400 |
0.58400 |
0.37100 |
| 329.15 |
0.59900 |
0.35100 |
0.58000 |
0.40200 |
| 330.25 |
0.68000 |
0.20000 |
0.63400 |
0.34700 |
| 330.35 |
0.82400 |
0.10200 |
0.73600 |
0.24800 |
| 340.25 |
0.19500 |
0.17400 |
0.15800 |
0.38600 |
| 331.25 |
0.20800 |
0.74500 |
0.35300 |
0.62200 |
| 340.65 |
0.11500 |
0.17900 |
0.08800 |
0.38200 |
| 345.45 |
0.17000 |
0.07200 |
0.14400 |
0.24100 |
| 341.95 |
0.48200 |
0.06700 |
0.48100 |
0.23500 |
| 330.35 |
0.29000 |
0.64400 |
0.42600 |
0.54000 |
| 331.65 |
0.20600 |
0.74000 |
0.34500 |
0.61700 |
| 341.65 |
0.47000 |
0.07100 |
0.46800 |
0.23500 |
| 339.55 |
0.54000 |
0.07500 |
0.54200 |
0.24400 |
| 332.25 |
0.45400 |
0.32500 |
0.46400 |
0.44000 |
| 333.75 |
0.73100 |
0.07700 |
0.70400 |
0.23000 |
| 329.05 |
0.56600 |
0.34200 |
0.58400 |
0.39100 |
| 338.95 |
0.24600 |
0.19700 |
0.20600 |
0.42000 |
| 335.55 |
0.03300 |
0.86100 |
0.05800 |
0.80900 |
| 335.75 |
0.03000 |
0.89800 |
0.05700 |
0.83800 |
| 337.55 |
0.07600 |
0.32800 |
0.05900 |
0.50600 |
| 329.75 |
0.32900 |
0.63900 |
0.46800 |
0.51700 |
(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 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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