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 2629
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 3 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 49.463 |
0.10000 |
0.20000 |
0.50000 |
0.12800 |
| 47.996 |
0.10000 |
0.40000 |
0.46900 |
0.23300 |
| 46.929 |
0.10000 |
0.50000 |
0.45700 |
0.29300 |
| 44.530 |
0.10000 |
0.70000 |
0.45200 |
0.39400 |
| 51.596 |
0.20000 |
0.20000 |
0.52600 |
0.12600 |
| 50.263 |
0.20000 |
0.40000 |
0.50500 |
0.23100 |
| 47.996 |
0.20000 |
0.60000 |
0.50200 |
0.34000 |
| 52.529 |
0.40000 |
0.20000 |
0.53500 |
0.14400 |
| 49.996 |
0.40000 |
0.40000 |
0.51900 |
0.28100 |
| 52.262 |
0.60000 |
0.20000 |
0.54100 |
0.18900 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Morachevskii A.G.; Komarova E.G.: Untersuchung des Dampf-Flüssig-Gleichgewichtes im System Benzol - Cyclohexan -Methanol. Vestn.Leningr.Univ. 12 (1957) 118-126 |
Vapor-Liquid Equilibrium Data Set 2633
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 3 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 95.459 |
0.10000 |
0.20000 |
0.52600 |
0.11800 |
| 91.192 |
0.10000 |
0.40000 |
0.48900 |
0.22400 |
| 89.993 |
0.10000 |
0.50000 |
0.47900 |
0.28000 |
| 85.060 |
0.10000 |
0.70000 |
0.47500 |
0.38000 |
| 100.392 |
0.20000 |
0.20000 |
0.55500 |
0.11800 |
| 97.325 |
0.20000 |
0.40000 |
0.54400 |
0.21300 |
| 92.659 |
0.20000 |
0.60000 |
0.52000 |
0.32800 |
| 101.725 |
0.40000 |
0.20000 |
0.55300 |
0.13900 |
| 97.325 |
0.40000 |
0.40000 |
0.55700 |
0.25900 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Morachevskii A.G.; Komarova E.G.: Untersuchung des Dampf-Flüssig-Gleichgewichtes im System Benzol - Cyclohexan -Methanol. Vestn.Leningr.Univ. 12 (1957) 118-126 |
Vapor-Liquid Equilibrium Data Set 13313
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 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] |
| 337.72 |
1.00000 |
0.00000 |
1.00000 |
0.00000 |
| 353.26 |
0.00000 |
1.00000 |
0.00000 |
1.00000 |
| 353.81 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
| 332.10 |
0.91700 |
0.06300 |
0.77800 |
0.13000 |
| 329.90 |
0.83600 |
0.12500 |
0.65600 |
0.21300 |
| 330.10 |
0.76400 |
0.19800 |
0.63800 |
0.26700 |
| 329.95 |
0.69400 |
0.27300 |
0.61000 |
0.31000 |
| 330.05 |
0.60600 |
0.35400 |
0.57300 |
0.32700 |
| 330.05 |
0.51900 |
0.43400 |
0.58300 |
0.34600 |
| 330.30 |
0.42700 |
0.52000 |
0.57900 |
0.35900 |
| 332.85 |
0.11600 |
0.25000 |
0.49400 |
0.15500 |
| 327.85 |
0.19400 |
0.23800 |
0.55200 |
0.13500 |
| 327.75 |
0.26600 |
0.22800 |
0.56100 |
0.12800 |
| 327.75 |
0.38000 |
0.21400 |
0.56500 |
0.14000 |
| 327.95 |
0.46000 |
0.20600 |
0.55900 |
0.14900 |
| 327.95 |
0.53200 |
0.19000 |
0.56200 |
0.15100 |
| 327.95 |
0.59700 |
0.17600 |
0.57000 |
0.15600 |
| 327.95 |
0.65100 |
0.16000 |
0.56400 |
0.15700 |
| 328.15 |
0.70700 |
0.14600 |
0.57800 |
0.16400 |
| 328.20 |
0.73700 |
0.12900 |
0.60800 |
0.15400 |
| 328.30 |
0.76400 |
0.11500 |
0.61600 |
0.14600 |
| 328.40 |
0.81300 |
0.08400 |
0.61500 |
0.11800 |
| 328.55 |
0.73600 |
0.16100 |
0.59900 |
0.19400 |
| 328.95 |
0.65000 |
0.24700 |
0.57700 |
0.24800 |
| 329.25 |
0.57400 |
0.32300 |
0.56900 |
0.27800 |
| 329.50 |
0.48900 |
0.40000 |
0.58200 |
0.27900 |
| 329.85 |
0.39000 |
0.48300 |
0.56000 |
0.31700 |
| 330.35 |
0.30100 |
0.55900 |
0.54300 |
0.33400 |
| 330.65 |
0.30700 |
0.58400 |
0.54100 |
0.36000 |
| 330.65 |
0.30200 |
0.62000 |
0.54600 |
0.37100 |
| 332.25 |
0.25000 |
0.70000 |
0.52800 |
0.41200 |
| 334.95 |
0.14800 |
0.79400 |
0.48200 |
0.46500 |
| 334.95 |
0.11200 |
0.53400 |
0.41500 |
0.33200 |
| 328.85 |
0.13900 |
0.24300 |
0.54800 |
0.14000 |
| 328.15 |
0.16600 |
0.21000 |
0.54900 |
0.11900 |
| 328.85 |
0.14200 |
0.24000 |
0.55400 |
0.13200 |
| 328.25 |
0.27200 |
0.31900 |
0.55100 |
0.19000 |
| 328.05 |
0.26100 |
0.29300 |
0.54900 |
0.17100 |
| 328.15 |
0.35600 |
0.27500 |
0.55600 |
0.17700 |
| 328.05 |
0.46500 |
0.24000 |
0.55300 |
0.17200 |
| 328.05 |
0.53000 |
0.22500 |
0.56100 |
0.17800 |
| 328.45 |
0.53100 |
0.26500 |
0.55800 |
0.21400 |
| 328.85 |
0.48100 |
0.34200 |
0.55400 |
0.25700 |
| 329.25 |
0.41100 |
0.42100 |
0.54600 |
0.28300 |
| 329.45 |
0.33100 |
0.49400 |
0.54400 |
0.30200 |
| 330.05 |
0.24000 |
0.60800 |
0.53100 |
0.34300 |
| 333.65 |
0.16700 |
0.68600 |
0.47800 |
0.40500 |
| 336.45 |
0.10100 |
0.77400 |
0.42500 |
0.47000 |
| 330.10 |
0.16000 |
0.43700 |
0.51100 |
0.24300 |
| 328.45 |
0.29400 |
0.38200 |
0.54500 |
0.22100 |
| 328.50 |
0.40400 |
0.33900 |
0.54800 |
0.22400 |
| 329.05 |
0.32200 |
0.44600 |
0.54100 |
0.26900 |
| 329.95 |
0.22100 |
0.55300 |
0.54200 |
0.29700 |
| 334.45 |
0.14700 |
0.62900 |
0.44300 |
0.38200 |
| 329.85 |
0.15000 |
0.52800 |
0.47200 |
0.31500 |
| 328.85 |
0.18300 |
0.42700 |
0.52600 |
0.22800 |
| 329.05 |
0.27300 |
0.45700 |
0.53500 |
0.26400 |
| 351.25 |
0.01300 |
0.94900 |
0.02400 |
0.92400 |
| 351.51 |
0.00900 |
0.89700 |
0.00400 |
0.87200 |
| 348.82 |
0.01600 |
0.81500 |
0.08000 |
0.73700 |
| 347.40 |
0.01400 |
0.60100 |
0.07600 |
0.54600 |
| 341.39 |
0.02700 |
0.50600 |
0.22100 |
0.39900 |
| 341.95 |
0.01600 |
0.43100 |
0.20700 |
0.34000 |
| 343.35 |
0.00500 |
0.36800 |
0.17800 |
0.31900 |
| 344.50 |
0.01000 |
0.30000 |
0.17000 |
0.26500 |
| 340.58 |
0.01800 |
0.26100 |
0.27500 |
0.21600 |
| 344.40 |
0.02100 |
0.67500 |
0.16500 |
0.54800 |
| 334.15 |
0.09000 |
0.45300 |
0.43400 |
0.28100 |
| 333.05 |
0.08400 |
0.38500 |
0.47300 |
0.22800 |
| 332.00 |
0.08000 |
0.32000 |
0.50400 |
0.18700 |
| 335.35 |
0.06100 |
0.59200 |
0.39400 |
0.36600 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Arce A.; Dominguez A.; Tojo J.: Vapor-Liquid Equilibrium of the System Methanol + Benzene + Cyclohexane at 760 mmHg. J.Chem.Eng.Data 35 (1990) 30-33 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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