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 2527
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
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] |
| 346.85 |
0.02100 |
0.94200 |
0.05700 |
0.85000 |
| 345.05 |
0.05800 |
0.90100 |
0.14600 |
0.77700 |
| 345.55 |
0.06100 |
0.91100 |
0.17100 |
0.77800 |
| 342.65 |
0.06400 |
0.87400 |
0.15200 |
0.70900 |
| 343.35 |
0.06700 |
0.83800 |
0.14600 |
0.69000 |
| 342.75 |
0.06700 |
0.84300 |
0.09900 |
0.69400 |
| 343.75 |
0.08200 |
0.86700 |
0.18800 |
0.71600 |
| 340.95 |
0.11500 |
0.68900 |
0.19400 |
0.60400 |
| 341.35 |
0.11900 |
0.70600 |
0.20400 |
0.59000 |
| 340.85 |
0.12000 |
0.73400 |
0.22800 |
0.61800 |
| 340.85 |
0.12100 |
0.74300 |
0.21900 |
0.61700 |
| 342.55 |
0.12200 |
0.83300 |
0.26000 |
0.68100 |
| 341.05 |
0.13100 |
0.55400 |
0.18300 |
0.57200 |
| 353.15 |
0.13900 |
0.00500 |
0.43100 |
0.17200 |
| 355.15 |
0.15800 |
0.01400 |
0.52600 |
0.04700 |
| 340.05 |
0.19600 |
0.72600 |
0.30200 |
0.59600 |
| 340.25 |
0.20400 |
0.52800 |
0.29000 |
0.52200 |
| 340.65 |
0.21600 |
0.37600 |
0.26900 |
0.51900 |
| 339.95 |
0.21900 |
0.56200 |
0.28900 |
0.52000 |
| 340.55 |
0.22000 |
0.38700 |
0.23500 |
0.54700 |
| 349.15 |
0.24800 |
0.01100 |
0.53600 |
0.15500 |
| 340.55 |
0.25400 |
0.29700 |
0.30100 |
0.48100 |
| 339.95 |
0.26000 |
0.43000 |
0.31200 |
0.49000 |
| 347.55 |
0.26200 |
0.00400 |
0.61400 |
0.06200 |
| 339.95 |
0.28700 |
0.35700 |
0.33300 |
0.46100 |
| 341.25 |
0.28900 |
0.13800 |
0.35600 |
0.41900 |
| 342.55 |
0.29400 |
0.06500 |
0.41300 |
0.34900 |
| 339.55 |
0.29700 |
0.42200 |
0.35000 |
0.46800 |
| 339.35 |
0.30400 |
0.46300 |
0.37900 |
0.48200 |
| 338.45 |
0.30600 |
0.63200 |
0.42900 |
0.51400 |
| 339.95 |
0.31300 |
0.32500 |
0.36100 |
0.44100 |
| 340.45 |
0.32400 |
0.21800 |
0.37400 |
0.42100 |
| 340.65 |
0.32800 |
0.18000 |
0.38300 |
0.41100 |
| 340.05 |
0.32900 |
0.28800 |
0.37100 |
0.42900 |
| 338.05 |
0.32900 |
0.59300 |
0.44500 |
0.48100 |
| 346.25 |
0.33000 |
0.01900 |
0.57200 |
0.17300 |
| 347.75 |
0.35700 |
0.00900 |
0.65400 |
0.08000 |
| 340.85 |
0.36800 |
0.13700 |
0.43400 |
0.35700 |
| 338.45 |
0.37800 |
0.44400 |
0.45700 |
0.43500 |
| 340.15 |
0.38100 |
0.20800 |
0.42700 |
0.38200 |
| 342.65 |
0.38500 |
0.05900 |
0.52200 |
0.26400 |
| 341.75 |
0.38800 |
0.08700 |
0.48800 |
0.30900 |
| 339.25 |
0.40500 |
0.27500 |
0.44500 |
0.39400 |
| 344.25 |
0.41900 |
0.03100 |
0.61300 |
0.17500 |
| 340.55 |
0.42500 |
0.13800 |
0.48600 |
0.32900 |
| 339.35 |
0.43800 |
0.22100 |
0.48000 |
0.36100 |
| 341.85 |
0.47100 |
0.06800 |
0.58000 |
0.23700 |
| 344.95 |
0.48700 |
0.01500 |
0.71400 |
0.08300 |
| 338.35 |
0.51400 |
0.25600 |
0.54400 |
0.33900 |
| 342.25 |
0.52400 |
0.05000 |
0.65400 |
0.17900 |
| 340.55 |
0.52800 |
0.09700 |
0.59400 |
0.25000 |
| 340.85 |
0.53300 |
0.08000 |
0.62200 |
0.22200 |
| 336.85 |
0.54700 |
0.36700 |
0.59500 |
0.35700 |
| 340.25 |
0.55200 |
0.10600 |
0.60500 |
0.24500 |
| 343.25 |
0.57000 |
0.02100 |
0.73500 |
0.08400 |
| 340.95 |
0.58900 |
0.06300 |
0.68000 |
0.17300 |
| 336.95 |
0.60800 |
0.28400 |
0.62100 |
0.31600 |
| 339.05 |
0.62600 |
0.12600 |
0.65900 |
0.23800 |
| 336.35 |
0.63900 |
0.28800 |
0.65600 |
0.30400 |
| 339.55 |
0.66600 |
0.08300 |
0.72000 |
0.18400 |
| 341.25 |
0.67000 |
0.02800 |
0.79700 |
0.08200 |
| 337.05 |
0.69700 |
0.17800 |
0.68100 |
0.26100 |
| 336.45 |
0.70700 |
0.21100 |
0.70800 |
0.25800 |
| 336.85 |
0.78300 |
0.13600 |
0.76900 |
0.19600 |
| 338.65 |
0.83000 |
0.04700 |
0.85800 |
0.08800 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Akita K.; Yoshida F.: Phase-Equilibria in Methanol-Ethyl Acetate-Water System. J.Chem.Eng.Data 8 (1963) 484-490 |
Vapor-Liquid Equilibrium Data Set 3552
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
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] |
| 335.85 |
0.71500 |
0.24100 |
0.69600 |
0.26600 |
| 343.10 |
0.75000 |
0.18200 |
0.73900 |
0.22300 |
| 336.20 |
0.58600 |
0.34100 |
0.62100 |
0.32800 |
| 336.55 |
0.64500 |
0.25600 |
0.64700 |
0.28900 |
| 336.55 |
0.55500 |
0.36700 |
0.59700 |
0.34200 |
| 336.90 |
0.43500 |
0.52300 |
0.54600 |
0.40500 |
| 337.10 |
0.78500 |
0.11200 |
0.78100 |
0.14200 |
| 337.15 |
0.46500 |
0.45000 |
0.53700 |
0.38200 |
| 337.25 |
0.50800 |
0.37300 |
0.55900 |
0.35500 |
| 337.50 |
0.52000 |
0.32800 |
0.55700 |
0.34300 |
| 337.60 |
0.68000 |
0.16300 |
0.68700 |
0.21600 |
| 337.65 |
0.35000 |
0.59900 |
0.47800 |
0.44800 |
| 337.90 |
0.36900 |
0.48600 |
0.45400 |
0.43000 |
| 338.00 |
0.84500 |
0.04600 |
0.86700 |
0.06300 |
| 338.20 |
0.40300 |
0.40300 |
0.45600 |
0.40000 |
| 338.25 |
0.55300 |
0.22500 |
0.58100 |
0.30800 |
| 338.30 |
0.30000 |
0.62600 |
0.43800 |
0.47300 |
| 338.50 |
0.23000 |
0.15300 |
0.49700 |
0.17200 |
| 338.70 |
0.48800 |
0.23600 |
0.52700 |
0.33100 |
| 338.85 |
0.60500 |
0.15100 |
0.63700 |
0.23100 |
| 338.95 |
0.26900 |
0.61000 |
0.38700 |
0.48600 |
| 339.00 |
0.63100 |
0.12900 |
0.66300 |
0.20000 |
| 339.00 |
0.69600 |
0.09300 |
0.73300 |
0.10000 |
| 339.05 |
0.33700 |
0.40700 |
0.38500 |
0.43600 |
| 339.15 |
0.23600 |
0.70900 |
0.40100 |
0.51700 |
| 339.55 |
0.39000 |
0.26000 |
0.43400 |
0.38000 |
| 339.55 |
0.27100 |
0.46100 |
0.33300 |
0.47200 |
| 339.60 |
0.71800 |
0.06000 |
0.77700 |
0.08200 |
| 339.80 |
0.31600 |
0.32500 |
0.36000 |
0.43800 |
| 339.95 |
0.43700 |
0.18100 |
0.49900 |
0.32300 |
| 340.05 |
0.33100 |
0.26600 |
0.37900 |
0.41500 |
| 340.05 |
0.63100 |
0.07300 |
0.70900 |
0.11200 |
| 340.05 |
0.38700 |
0.20800 |
0.44300 |
0.36200 |
| 340.40 |
0.50600 |
0.10400 |
0.60100 |
0.20600 |
| 340.45 |
0.44500 |
0.12600 |
0.53800 |
0.27700 |
| 340.70 |
0.75000 |
0.02200 |
0.84700 |
0.03000 |
| 340.75 |
0.53600 |
0.07800 |
0.64700 |
0.15400 |
| 340.75 |
0.27000 |
0.23400 |
0.32900 |
0.45800 |
| 340.80 |
0.12500 |
0.70300 |
0.20000 |
0.57400 |
| 341.00 |
0.65000 |
0.04100 |
0.76300 |
0.05700 |
| 341.15 |
0.50500 |
0.06400 |
0.63000 |
0.15400 |
| 341.65 |
0.25200 |
0.15200 |
0.35000 |
0.44600 |
| 342.35 |
0.67600 |
0.01300 |
0.82200 |
0.01600 |
| 343.15 |
0.55500 |
0.03600 |
0.72300 |
0.06900 |
| 345.20 |
0.39200 |
0.04000 |
0.58200 |
0.16800 |
| 346.25 |
0.33000 |
0.03500 |
0.54300 |
0.17700 |
| 346.40 |
0.32100 |
0.04000 |
0.53000 |
0.16900 |
| 346.40 |
0.26800 |
0.05600 |
0.45700 |
0.31300 |
| 347.20 |
0.22800 |
0.04700 |
0.43300 |
0.32500 |
| 342.25 |
0.36100 |
0.08700 |
0.49500 |
0.28200 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| van Zandijcke F.; Verhoeye L.: The Vapor-Liquid Equilibrium of Ternary Systems with Limited Miscibility at Atmospheric Pressure. J.Appl.Chem.Biotechnol. 24 (1974) 709-729 |
List of All References
Vapor-Liquid Equilibrium Data Overview
© DDBST GmbH