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 6444
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 3 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
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] |
| 350.55 |
0.05300 |
0.07900 |
0.11200 |
0.08700 |
| 350.25 |
0.05500 |
0.15200 |
0.10700 |
0.16700 |
| 349.85 |
0.05800 |
0.23800 |
0.10000 |
0.24700 |
| 349.55 |
0.06300 |
0.36600 |
0.09700 |
0.35900 |
| 349.65 |
0.06500 |
0.44700 |
0.09100 |
0.43000 |
| 349.85 |
0.07000 |
0.56000 |
0.09000 |
0.52500 |
| 350.25 |
0.06600 |
0.63100 |
0.08300 |
0.59000 |
| 350.45 |
0.07000 |
0.69100 |
0.08700 |
0.64400 |
| 350.85 |
0.07300 |
0.76100 |
0.08800 |
0.71300 |
| 351.15 |
0.07200 |
0.79000 |
0.08300 |
0.74400 |
| 352.05 |
0.06400 |
0.87300 |
0.07400 |
0.84100 |
| 348.55 |
0.12000 |
0.09700 |
0.21100 |
0.09800 |
| 348.45 |
0.12300 |
0.17700 |
0.19900 |
0.17200 |
| 348.35 |
0.13400 |
0.23900 |
0.20100 |
0.22800 |
| 348.45 |
0.13700 |
0.33100 |
0.19000 |
0.30500 |
| 348.65 |
0.13900 |
0.39700 |
0.18300 |
0.36300 |
| 348.75 |
0.14600 |
0.46000 |
0.18400 |
0.41500 |
| 349.25 |
0.13200 |
0.55000 |
0.16100 |
0.50000 |
| 349.75 |
0.13500 |
0.62500 |
0.15800 |
0.56800 |
| 350.15 |
0.13500 |
0.68200 |
0.15700 |
0.62500 |
| 350.75 |
0.13000 |
0.74900 |
0.14900 |
0.69700 |
| 351.65 |
0.12500 |
0.81700 |
0.14400 |
0.77900 |
| 347.15 |
0.19200 |
0.09900 |
0.28700 |
0.09200 |
| 347.45 |
0.18300 |
0.19700 |
0.25700 |
0.17800 |
| 347.45 |
0.20000 |
0.25600 |
0.26100 |
0.22700 |
| 347.75 |
0.20000 |
0.33000 |
0.25000 |
0.29200 |
| 348.15 |
0.20600 |
0.39600 |
0.24700 |
0.34700 |
| 348.55 |
0.20000 |
0.48700 |
0.23200 |
0.42900 |
| 349.05 |
0.19700 |
0.56100 |
0.22400 |
0.49800 |
| 349.95 |
0.18400 |
0.64700 |
0.20900 |
0.58500 |
| 350.55 |
0.17100 |
0.71200 |
0.19300 |
0.65700 |
| 351.25 |
0.18000 |
0.76200 |
0.20200 |
0.71900 |
| 346.35 |
0.27000 |
0.09500 |
0.35200 |
0.08100 |
| 346.65 |
0.26600 |
0.17300 |
0.33400 |
0.14700 |
| 346.85 |
0.28400 |
0.25400 |
0.33400 |
0.21400 |
| 347.45 |
0.25500 |
0.33500 |
0.29800 |
0.28700 |
| 347.95 |
0.27700 |
0.41000 |
0.30700 |
0.35100 |
| 348.55 |
0.27000 |
0.48700 |
0.29500 |
0.42300 |
| 349.05 |
0.26600 |
0.55000 |
0.29000 |
0.48600 |
| 350.05 |
0.26300 |
0.62000 |
0.28500 |
0.56100 |
| 350.75 |
0.27300 |
0.67000 |
0.29700 |
0.62300 |
| 345.85 |
0.35000 |
0.10000 |
0.40800 |
0.08100 |
| 346.25 |
0.35000 |
0.18000 |
0.39200 |
0.14800 |
| 346.65 |
0.35500 |
0.25100 |
0.38600 |
0.20700 |
| 347.35 |
0.34600 |
0.34900 |
0.36900 |
0.29300 |
| 347.95 |
0.35500 |
0.41200 |
0.37300 |
0.35000 |
| 348.75 |
0.34300 |
0.48600 |
0.36000 |
0.42400 |
| 349.35 |
0.34200 |
0.53300 |
0.36100 |
0.47400 |
| 350.35 |
0.33600 |
0.60200 |
0.35600 |
0.55500 |
| 345.45 |
0.44000 |
0.09300 |
0.46600 |
0.07400 |
| 346.05 |
0.43500 |
0.17500 |
0.45300 |
0.14000 |
| 346.95 |
0.41200 |
0.29000 |
0.42500 |
0.23900 |
| 347.35 |
0.43000 |
0.32200 |
0.43700 |
0.26900 |
| 348.35 |
0.42200 |
0.40800 |
0.43000 |
0.35200 |
| 349.05 |
0.41000 |
0.47500 |
0.42200 |
0.42100 |
| 350.15 |
0.40700 |
0.53500 |
0.42500 |
0.49100 |
| 345.45 |
0.52000 |
0.09200 |
0.51600 |
0.07200 |
| 346.15 |
0.52000 |
0.17400 |
0.51100 |
0.14000 |
| 346.75 |
0.49000 |
0.25300 |
0.48500 |
0.20700 |
| 347.65 |
0.50000 |
0.32000 |
0.49500 |
0.27200 |
| 348.65 |
0.49500 |
0.38900 |
0.49700 |
0.34000 |
| 349.75 |
0.48700 |
0.45300 |
0.49800 |
0.41400 |
| 345.65 |
0.60300 |
0.09100 |
0.57300 |
0.07200 |
| 346.55 |
0.59400 |
0.17700 |
0.56900 |
0.14400 |
| 347.25 |
0.58700 |
0.23800 |
0.56700 |
0.20000 |
| 349.45 |
0.55900 |
0.38200 |
0.56100 |
0.34800 |
| 346.05 |
0.66600 |
0.09200 |
0.62000 |
0.07500 |
| 346.95 |
0.66100 |
0.16800 |
0.62500 |
0.14000 |
| 348.15 |
0.64700 |
0.24200 |
0.62400 |
0.21000 |
| 349.15 |
0.63300 |
0.30900 |
0.62800 |
0.28000 |
| 346.65 |
0.74400 |
0.08500 |
0.68700 |
0.07200 |
| 347.75 |
0.73000 |
0.16000 |
0.69400 |
0.13900 |
| 348.95 |
0.70600 |
0.23500 |
0.69000 |
0.21300 |
| 347.65 |
0.80200 |
0.08900 |
0.75300 |
0.07700 |
| 348.85 |
0.78800 |
0.15500 |
0.76500 |
0.14200 |
| 348.65 |
0.86000 |
0.08500 |
0.82600 |
0.07800 |
| 344.85 |
0.53500 |
0.02900 |
0.53400 |
0.02300 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Chao K.-C.: Vapor-Liquid Equilibria in the Ternary System Ethyl Acetate-Benzene-Cyclohexane. Thesis (1956) |
List of All References
Vapor-Liquid Equilibrium Data Overview
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