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 1621
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
| 2 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 5.306 |
0.00650 |
0.13430 |
| 19.678 |
0.14460 |
0.78580 |
| 24.065 |
0.20830 |
0.83740 |
| 27.104 |
0.26630 |
0.86110 |
| 31.357 |
0.39540 |
0.88910 |
| 34.264 |
0.55580 |
0.90840 |
| 35.864 |
0.68920 |
0.91990 |
| 36.597 |
0.78070 |
0.92670 |
| 37.024 |
0.84180 |
0.93430 |
| 37.277 |
0.89000 |
0.93830 |
| 37.370 |
0.94870 |
0.95120 |
| 37.437 |
0.95890 |
0.95330 |
| 37.357 |
0.97040 |
0.95820 |
| 36.704 |
0.99640 |
0.99100 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Vonka P.; Svoboda V.; Strubl K.; Holub R.: XLVI System Cyclohexane-1-Butanol at 50 and 70°C. Collect.Czech.Chem.Commun. 36 (1971) 18-34 |
Vapor-Liquid Equilibrium Data Set 1622
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
| 2 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 18.865 |
0.02130 |
0.28180 |
| 25.398 |
0.05920 |
0.48440 |
| 37.677 |
0.12050 |
0.66480 |
| 44.716 |
0.17210 |
0.73240 |
| 50.463 |
0.21220 |
0.76750 |
| 59.742 |
0.31790 |
0.82420 |
| 63.968 |
0.39830 |
0.83650 |
| 67.114 |
0.46090 |
0.85450 |
| 72.701 |
0.66010 |
0.88120 |
| 74.861 |
0.78030 |
0.90660 |
| 75.540 |
0.88600 |
0.91870 |
| 76.127 |
0.89550 |
0.91740 |
| 75.767 |
0.92280 |
0.92370 |
| 75.554 |
0.96910 |
0.94750 |
| 74.634 |
0.98330 |
0.97200 |
| 74.541 |
0.98470 |
0.97340 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Vonka P.; Svoboda V.; Strubl K.; Holub R.: XLVI System Cyclohexane-1-Butanol at 50 and 70°C. Collect.Czech.Chem.Commun. 36 (1971) 18-34 |
Vapor-Liquid Equilibrium Data Set 2178
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
| 2 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 77.754 |
0.00000 |
0.00000 |
| 121.107 |
0.10000 |
0.41170 |
| 153.897 |
0.20000 |
0.57790 |
| 178.521 |
0.30000 |
0.65630 |
| 196.896 |
0.40000 |
0.70170 |
| 210.448 |
0.50000 |
0.75220 |
| 220.123 |
0.60000 |
0.77920 |
| 226.387 |
0.70000 |
0.79840 |
| 229.212 |
0.80000 |
0.82610 |
| 228.093 |
0.90000 |
0.87500 |
| 222.040 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Ramalho R.S.; Delmas J.: Isothermal and Isobaric Vapor-Liquid Equilibrium Data and Excess Free Energies by the Total Pressure Method. J.Chem.Eng.Data 13 (1968) 161-164 |
Diagrams
List of All References
| Source |
| Vonka P.; Svoboda V.; Strubl K.; Holub R.: XLVI System Cyclohexane-1-Butanol at 50 and 70°C. Collect.Czech.Chem.Commun. 36 (1971) 18-34 |
| Ramalho R.S.; Delmas J.: Isothermal and Isobaric Vapor-Liquid Equilibrium Data and Excess Free Energies by the Total Pressure Method. J.Chem.Eng.Data 13 (1968) 161-164 |
Vapor-Liquid Equilibrium Data Overview
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