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 521
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 351.45 |
0.00000 |
0.00000 |
| 349.15 |
0.01000 |
0.09500 |
| 346.35 |
0.02000 |
0.19300 |
| 340.55 |
0.06000 |
0.36500 |
| 339.05 |
0.08000 |
0.42000 |
| 334.95 |
0.15200 |
0.53200 |
| 332.55 |
0.24500 |
0.60500 |
| 331.85 |
0.33300 |
0.63000 |
| 331.50 |
0.45200 |
0.64000 |
| 331.25 |
0.58800 |
0.65000 |
| 331.15 |
0.67000 |
0.66000 |
| 331.40 |
0.72500 |
0.67000 |
| 331.60 |
0.76500 |
0.67500 |
| 332.30 |
0.89800 |
0.71000 |
| 333.35 |
0.95500 |
0.74500 |
| 336.65 |
0.99000 |
0.84000 |
| 339.85 |
0.99400 |
0.93500 |
| 341.85 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Sinor J.E.; Weber J.H.: Vapor-Liquid Equilibria at Atmospheric Pressure. Systems Containing Ethyl Alcohol, n-Hexane, Benzene and Methylcyclopentane. J.Chem.Eng.Data 5 (1960) 243-247 |
Vapor-Liquid Equilibrium Data Set 710
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 46.036 |
0.01100 |
0.17800 |
| 65.488 |
0.07000 |
0.43100 |
| 71.794 |
0.10000 |
0.48700 |
| 78.447 |
0.14100 |
0.52000 |
| 83.193 |
0.20600 |
0.56800 |
| 87.246 |
0.30300 |
0.58300 |
| 88.033 |
0.33200 |
0.59500 |
| 89.113 |
0.38700 |
0.60600 |
| 89.753 |
0.40900 |
0.60900 |
| 89.926 |
0.49800 |
0.62100 |
| 90.193 |
0.53700 |
0.62200 |
| 90.219 |
0.60300 |
0.63500 |
| 89.939 |
0.72400 |
0.65000 |
| 89.793 |
0.81000 |
0.68200 |
| 87.313 |
0.90000 |
0.70400 |
| 85.393 |
0.94300 |
0.74600 |
| 80.260 |
0.96100 |
0.80200 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Yuan K.S.; Lu B.C-Y.; Deshpande A.K.; Ho J.C.K.: Part III. System Ethanol - Cyclohexane at Atmospheric Pressure. J.Chem.Eng.Data 8 (1963) 549-559 |
Vapor-Liquid Equilibrium Data Set 711
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 2.3065 |
0.05000 |
0.64740 |
| 3.100 |
0.10000 |
0.74410 |
| 3.504 |
0.15000 |
0.77930 |
| 3.738 |
0.20000 |
0.79780 |
| 3.884 |
0.25000 |
0.80670 |
| 3.980 |
0.30000 |
0.81240 |
| 4.040 |
0.35000 |
0.81510 |
| 4.089 |
0.40000 |
0.81840 |
| 4.126 |
0.45000 |
0.82070 |
| 4.160 |
0.50000 |
0.82210 |
| 4.189 |
0.55000 |
0.82330 |
| 4.208 |
0.60000 |
0.82480 |
| 4.220 |
0.65000 |
0.82620 |
| 4.221 |
0.70000 |
0.82750 |
| 4.213 |
0.75000 |
0.82910 |
| 4.197 |
0.80000 |
0.83230 |
| 4.157 |
0.85000 |
0.84020 |
| 4.090 |
0.90000 |
0.85660 |
| 3.990 |
0.95000 |
0.88970 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Ishii N.: Studies on Volatility of Fuels Containing Ethyl Alcohol V-VI. J.Soc.Chem.Ind.Jap. 38 (1935) 659-25271068 |
Diagrams
List of All References
| Source |
| Sinor J.E.; Weber J.H.: Vapor-Liquid Equilibria at Atmospheric Pressure. Systems Containing Ethyl Alcohol, n-Hexane, Benzene and Methylcyclopentane. J.Chem.Eng.Data 5 (1960) 243-247 |
| Ishii N.: Studies on Volatility of Fuels Containing Ethyl Alcohol V-VI. J.Soc.Chem.Ind.Jap. 38 (1935) 659-165387808 |
| Yuan K.S.; Lu B.C-Y.; Deshpande A.K.; Ho J.C.K.: Part III. System Ethanol - Cyclohexane at Atmospheric Pressure. J.Chem.Eng.Data 8 (1963) 549-559 |
Vapor-Liquid Equilibrium Data Overview
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