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 3829
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 3 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
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] |
| 344.65 |
0.01200 |
0.37850 |
0.02850 |
0.47500 |
| 346.40 |
0.01340 |
0.20670 |
0.06340 |
0.36670 |
| 344.20 |
0.01650 |
0.37340 |
0.05200 |
0.46340 |
| 346.20 |
0.02340 |
0.19330 |
0.09000 |
0.33340 |
| 344.45 |
0.02340 |
0.38850 |
0.04000 |
0.46850 |
| 345.85 |
0.03000 |
0.19500 |
0.09700 |
0.32340 |
| 344.00 |
0.03000 |
0.37160 |
0.08000 |
0.45500 |
| 345.05 |
0.03160 |
0.18670 |
0.14000 |
0.32000 |
| 345.15 |
0.03160 |
0.19000 |
0.14000 |
0.33340 |
| 345.40 |
0.03340 |
0.19330 |
0.12670 |
0.33000 |
| 345.05 |
0.03670 |
0.19500 |
0.14000 |
0.32000 |
| 345.15 |
0.03670 |
0.19660 |
0.13000 |
0.32500 |
| 343.55 |
0.03670 |
0.36170 |
0.10840 |
0.44500 |
| 344.40 |
0.04670 |
0.20000 |
0.16340 |
0.32670 |
| 343.25 |
0.05340 |
0.35500 |
0.13340 |
0.43200 |
| 344.00 |
0.05670 |
0.21600 |
0.17000 |
0.32340 |
| 343.85 |
0.06000 |
0.22000 |
0.16670 |
0.31850 |
| 343.70 |
0.06170 |
0.22170 |
0.17000 |
0.32000 |
| 343.35 |
0.06340 |
0.22340 |
0.19110 |
0.32670 |
| 343.80 |
0.06380 |
0.21000 |
0.21000 |
0.28900 |
| 343.35 |
0.07000 |
0.21670 |
0.20340 |
0.31670 |
| 342.75 |
0.07000 |
0.34000 |
0.16670 |
0.40680 |
| 343.00 |
0.07200 |
0.23000 |
0.20000 |
0.32670 |
| 342.70 |
0.07500 |
0.24000 |
0.20500 |
0.32750 |
| 343.00 |
0.08000 |
0.15670 |
0.26000 |
0.24670 |
| 342.45 |
0.08300 |
0.24500 |
0.21340 |
0.33000 |
| 342.60 |
0.08670 |
0.13660 |
0.29000 |
0.21340 |
| 341.85 |
0.09000 |
0.32340 |
0.20340 |
0.37850 |
| 342.50 |
0.09670 |
0.11500 |
0.31340 |
0.19000 |
| 342.00 |
0.09670 |
0.24170 |
0.24500 |
0.32000 |
| 341.55 |
0.10180 |
0.30680 |
0.23650 |
0.36500 |
| 340.90 |
0.12000 |
0.28160 |
0.27670 |
0.33000 |
| 339.95 |
0.15160 |
0.26340 |
0.32340 |
0.29000 |
| 339.25 |
0.18500 |
0.23000 |
0.36680 |
0.25170 |
| 339.30 |
0.18500 |
0.24680 |
0.36000 |
0.26200 |
| 338.85 |
0.21200 |
0.25600 |
0.38500 |
0.26340 |
| 338.60 |
0.22800 |
0.27150 |
0.38680 |
0.27000 |
| 338.30 |
0.25680 |
0.29340 |
0.39680 |
0.26670 |
| 338.15 |
0.27000 |
0.31840 |
0.40160 |
0.28000 |
| 337.80 |
0.30000 |
0.31170 |
0.41070 |
0.27000 |
| 337.65 |
0.32200 |
0.30340 |
0.44170 |
0.26670 |
| 338.00 |
0.34000 |
0.29000 |
0.44670 |
0.24850 |
| 337.00 |
0.37670 |
0.37000 |
0.48500 |
0.23000 |
| 336.75 |
0.41500 |
0.24850 |
0.50850 |
0.21340 |
| 336.45 |
0.46000 |
0.23670 |
0.53000 |
0.19150 |
| 336.15 |
0.51100 |
0.20330 |
0.56170 |
0.17000 |
| 336.00 |
0.55670 |
0.17340 |
0.59000 |
0.11160 |
| 335.80 |
0.61670 |
0.14680 |
0.61670 |
0.12000 |
| 335.65 |
0.65000 |
0.11670 |
0.65330 |
0.10000 |
| 335.65 |
0.69000 |
0.09680 |
0.67680 |
0.08670 |
| 335.50 |
0.73340 |
0.07850 |
0.68680 |
0.06000 |
| 335.60 |
0.74000 |
0.07340 |
0.69680 |
0.07000 |
| 335.65 |
0.77500 |
0.07000 |
0.71160 |
0.05850 |
| 335.45 |
0.77850 |
0.06000 |
0.71000 |
0.05340 |
| 335.85 |
0.80850 |
0.04160 |
0.73000 |
0.05330 |
| 336.35 |
0.88250 |
0.03000 |
0.79000 |
0.02670 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Govindaswamy S.; Andiappan A.; Lakshmanan S.: Isobaric Vapour-Liquid Equilibrium Data for the Ternary and Sub-Binary Systems Containing n-Hexane(1)-Benzene(2)- Isopropanol(3). J.Chem.Eng.Japan 9 (1976) 345-349 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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