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 6
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 |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 65.808 |
0.04050 |
0.35180 |
| 72.754 |
0.06380 |
0.42100 |
| 75.340 |
0.07710 |
0.44620 |
| 86.366 |
0.22980 |
0.54220 |
| 90.433 |
0.59880 |
0.60560 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Scatchard G.; Ticknor L.B.: IX. The Methanol-Carbon Tetrachloride-Benzene System. J.Am.Chem.Soc. 74 (1952) 3724-3729 |
Vapor-Liquid Equilibrium Data Set 18
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 |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 248.646 |
0.11700 |
0.50200 |
| 281.710 |
0.25700 |
0.59400 |
| 295.709 |
0.37600 |
0.61800 |
| 303.042 |
0.54900 |
0.65000 |
| 305.575 |
0.70700 |
0.68900 |
| 294.376 |
0.85600 |
0.76500 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Jost W.; Roeck H.; Schroeder W.; Sieg L.; Wagner H.G.: Apparatur zur Messung von Dampf-Flüssigkeits-Gleichgewichten bei Überdruck. Z.Phys.Chem.(München) 10 (1957) 133-136 |
Vapor-Liquid Equilibrium Data Set 39
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 |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 351.76 |
0.00200 |
0.04100 |
| 350.80 |
0.00280 |
0.06600 |
| 350.67 |
0.00300 |
0.06840 |
| 350.43 |
0.00300 |
0.08120 |
| 350.37 |
0.00410 |
0.08200 |
| 349.20 |
0.00550 |
0.11720 |
| 348.45 |
0.00580 |
0.13860 |
| 346.92 |
0.01340 |
0.19240 |
| 346.21 |
0.01900 |
0.20600 |
| 344.11 |
0.02760 |
0.26580 |
| 341.10 |
0.04600 |
0.33920 |
| 340.90 |
0.04800 |
0.34400 |
| 337.17 |
0.08300 |
0.43000 |
| 334.23 |
0.14370 |
0.49980 |
| 334.19 |
0.17000 |
0.51800 |
| 333.07 |
0.18580 |
0.52120 |
| 332.55 |
0.27600 |
0.54420 |
| 331.58 |
0.36400 |
0.57360 |
| 331.30 |
0.45580 |
0.58700 |
| 331.19 |
0.52400 |
0.59810 |
| 331.12 |
0.59700 |
0.61140 |
| 331.12 |
0.63700 |
0.62000 |
| 331.13 |
0.67390 |
0.62900 |
| 331.14 |
0.68000 |
0.63220 |
| 331.20 |
0.70240 |
0.64080 |
| 331.21 |
0.70710 |
0.64160 |
| 331.28 |
0.72980 |
0.65090 |
| 331.37 |
0.74400 |
0.65310 |
| 331.60 |
0.77680 |
0.66910 |
| 331.80 |
0.80310 |
0.68380 |
| 332.14 |
0.83800 |
0.70900 |
| 332.75 |
0.87540 |
0.74800 |
| 333.33 |
0.89980 |
0.77420 |
| 333.75 |
0.91780 |
0.80020 |
| 334.05 |
0.92500 |
0.81180 |
| 334.79 |
0.94240 |
0.85100 |
| 335.75 |
0.96520 |
0.89980 |
| 336.72 |
0.98490 |
0.94920 |
| 336.87 |
0.98800 |
0.95720 |
| 336.93 |
0.98900 |
0.96100 |
| 337.10 |
0.99180 |
0.96840 |
| 337.36 |
0.99490 |
0.97990 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Ocon J.; Espantoso J.: Equilibrio Vapor-Liquido. Anal.Fis.Quim.Ser.B 54 (1958) 421-430 |
Diagrams
List of All References
| Source |
| Scatchard G.; Ticknor L.B.: IX. The Methanol-Carbon Tetrachloride-Benzene System. J.Am.Chem.Soc. 74 (1952) 3724-3729 |
| Ocon J.; Espantoso J.: Equilibrio Vapor-Liquido. Anal.Fis.Quim.Ser.B 54 (1958) 421-430 |
| Jost W.; Roeck H.; Schroeder W.; Sieg L.; Wagner H.G.: Apparatur zur Messung von Dampf-Flüssigkeits-Gleichgewichten bei Überdruck. Z.Phys.Chem.(München) 10 (1957) 133-136 |
Vapor-Liquid Equilibrium Data Overview
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