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 2605
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 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] |
| 350.75 |
0.05500 |
0.93000 |
0.13600 |
0.81500 |
| 350.95 |
0.01500 |
0.88500 |
0.03900 |
0.81400 |
| 350.45 |
0.03000 |
0.83000 |
0.08500 |
0.73900 |
| 345.55 |
0.08500 |
0.71500 |
0.18600 |
0.57400 |
| 341.35 |
0.18500 |
0.65500 |
0.36800 |
0.46600 |
| 342.65 |
0.12500 |
0.61500 |
0.28200 |
0.45700 |
| 342.85 |
0.11000 |
0.57000 |
0.26900 |
0.43200 |
| 344.65 |
0.07500 |
0.52500 |
0.20100 |
0.43000 |
| 340.05 |
0.16500 |
0.46500 |
0.35400 |
0.31600 |
| 337.95 |
0.22000 |
0.43000 |
0.45900 |
0.26200 |
| 335.55 |
0.31500 |
0.37500 |
0.55200 |
0.20400 |
| 334.25 |
0.37000 |
0.34000 |
0.59100 |
0.17700 |
| 331.45 |
0.49000 |
0.27500 |
0.66100 |
0.13100 |
| 333.25 |
0.42000 |
0.33500 |
0.61800 |
0.17600 |
| 334.45 |
0.40300 |
0.38000 |
0.60500 |
0.20800 |
| 336.55 |
0.35500 |
0.48500 |
0.55900 |
0.27600 |
| 337.85 |
0.30500 |
0.54000 |
0.51700 |
0.33400 |
| 337.15 |
0.34500 |
0.52000 |
0.54600 |
0.31000 |
| 335.75 |
0.40000 |
0.47000 |
0.59200 |
0.28100 |
| 333.65 |
0.53500 |
0.37500 |
0.68100 |
0.21500 |
| 332.95 |
0.59000 |
0.32500 |
0.70500 |
0.17500 |
| 332.65 |
0.63500 |
0.30500 |
0.73800 |
0.17400 |
| 331.95 |
0.58500 |
0.28500 |
0.70200 |
0.13200 |
| 330.95 |
0.53500 |
0.26000 |
0.68700 |
0.11600 |
| 330.95 |
0.48500 |
0.23500 |
0.66500 |
0.10200 |
| 331.05 |
0.43000 |
0.21500 |
0.65000 |
0.09600 |
| 331.55 |
0.36500 |
0.19500 |
0.62500 |
0.08400 |
| 333.65 |
0.31000 |
0.25500 |
0.58500 |
0.12200 |
| 335.75 |
0.27000 |
0.34100 |
0.52000 |
0.19400 |
| 336.85 |
0.22500 |
0.31500 |
0.48200 |
0.18300 |
| 338.05 |
0.17000 |
0.28000 |
0.42700 |
0.17400 |
| 340.35 |
0.13100 |
0.33600 |
0.33600 |
0.24500 |
| 342.05 |
0.10200 |
0.41500 |
0.28000 |
0.31400 |
| 342.25 |
0.09500 |
0.37000 |
0.26200 |
0.29100 |
| 329.15 |
0.91100 |
0.06500 |
0.88000 |
0.02200 |
| 329.95 |
0.83500 |
0.13000 |
0.82600 |
0.05700 |
| 330.85 |
0.76000 |
0.20000 |
0.80100 |
0.10200 |
| 329.55 |
0.72000 |
0.18000 |
0.77200 |
0.08400 |
| 328.95 |
0.68000 |
0.17500 |
0.74800 |
0.07500 |
| 327.95 |
0.70000 |
0.13500 |
0.75400 |
0.05500 |
| 327.85 |
0.74500 |
0.11500 |
0.76800 |
0.04400 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Rao V.K.K.; Krishnamurty V.V.G.; Rao C.V.: Vapour-Liquid Equilibria: System Acetone 1 Benzene 2 Cyclohexane 3. Recl.Trav.Chim.Pays-Bas 76 (1957) 769-778 |
Vapor-Liquid Equilibrium Data Set 7285
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 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
| x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 0.66367 |
0.08408 |
0.73118 |
0.04233 |
| 0.62102 |
0.11112 |
0.72035 |
0.05081 |
| 0.36022 |
0.22459 |
0.54736 |
0.12828 |
| 0.17126 |
0.32827 |
0.38276 |
0.21366 |
| 0.10500 |
0.36801 |
0.31639 |
0.25046 |
| 0.48813 |
0.09163 |
0.70614 |
0.03774 |
| 0.26552 |
0.14757 |
0.48281 |
0.09542 |
| 0.09298 |
0.18778 |
0.22220 |
0.18004 |
| 0.04932 |
0.17180 |
0.10225 |
0.20546 |
| 0.017135 |
0.12951 |
0.03954 |
0.18373 |
| 0.71515 |
0.08404 |
0.75606 |
0.02469 |
| 0.68035 |
0.14680 |
0.72327 |
0.07800 |
| 0.52116 |
0.31981 |
0.66832 |
0.17403 |
| 0.33178 |
0.50725 |
0.50715 |
0.32319 |
| 0.19878 |
0.66314 |
0.36608 |
0.46066 |
(x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Vitman T.A.; Markova F.P.; Zharov V.T.: Investigation of Liquid-Vapor Equilibrium in the Four Component System Acetone-Benzene-Toluene-Cyclohexane. J.Appl.Chem.USSR 42 (1969) 2218-2221 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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