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 2109
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
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] |
y1 [mol/mol] |
| 353.87 |
0.00000 |
0.00000 |
| 352.65 |
0.08200 |
0.12100 |
| 352.15 |
0.12100 |
0.16700 |
| 351.35 |
0.16700 |
0.22600 |
| 350.50 |
0.22600 |
0.30000 |
| 349.90 |
0.27000 |
0.35300 |
| 349.55 |
0.30000 |
0.38400 |
| 348.85 |
0.35300 |
0.43800 |
| 348.55 |
0.38400 |
0.46800 |
| 347.85 |
0.43800 |
0.52300 |
| 346.85 |
0.52300 |
0.60200 |
| 346.05 |
0.59100 |
0.67100 |
| 345.20 |
0.67100 |
0.74000 |
| 344.55 |
0.74000 |
0.79200 |
| 344.00 |
0.79700 |
0.84000 |
| 343.55 |
0.84000 |
0.87700 |
| 343.20 |
0.87700 |
0.90400 |
| 341.85 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Ridgway K.; Butler P.A.: Some Physical Properties of the Ternary System Benzene-Cyclohexane-n-Hexane. J.Chem.Eng.Data 12 (1967) 509-515 |
Vapor-Liquid Equilibrium Data Set 3009
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 77.327 |
0.12500 |
0.17900 |
| 81.607 |
0.25000 |
0.33600 |
| 85.673 |
0.37500 |
0.46500 |
| 90.033 |
0.50000 |
0.59000 |
| 94.019 |
0.62500 |
0.70800 |
| 97.965 |
0.74200 |
0.80600 |
| 100.818 |
0.87500 |
0.90100 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Susarev M.P.; Chen S.T.: The Benzene-n-Hexane-Cyclo-Hexane System. Russ.J.Phys.Chem. 37 (1963) 938-943 |
Vapor-Liquid Equilibrium Data Set 4202
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
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] |
y1 [mol/mol] |
| 353.95 |
0.00000 |
0.00000 |
| 353.75 |
0.00800 |
0.01800 |
| 353.50 |
0.01900 |
0.03200 |
| 353.15 |
0.04500 |
0.07000 |
| 352.90 |
0.06300 |
0.09750 |
| 352.45 |
0.09350 |
0.13500 |
| 351.80 |
0.13300 |
0.18700 |
| 351.15 |
0.18150 |
0.24700 |
| 350.30 |
0.23850 |
0.31600 |
| 349.65 |
0.28700 |
0.37300 |
| 349.20 |
0.31800 |
0.40000 |
| 348.50 |
0.36900 |
0.45750 |
| 347.95 |
0.41450 |
0.50500 |
| 347.65 |
0.44250 |
0.53350 |
| 347.40 |
0.46200 |
0.55300 |
| 346.90 |
0.49800 |
0.58350 |
| 346.75 |
0.51550 |
0.59950 |
| 346.55 |
0.53550 |
0.61750 |
| 346.40 |
0.54900 |
0.63000 |
| 345.90 |
0.59550 |
0.67300 |
| 345.25 |
0.65450 |
0.72400 |
| 344.85 |
0.69250 |
0.75750 |
| 344.55 |
0.72400 |
0.78600 |
| 344.10 |
0.75700 |
0.80800 |
| 344.05 |
0.76850 |
0.81800 |
| 343.95 |
0.77700 |
0.82950 |
| 343.70 |
0.80700 |
0.85200 |
| 343.50 |
0.83100 |
0.87150 |
| 343.30 |
0.85000 |
0.88300 |
| 343.10 |
0.87350 |
0.90200 |
| 342.90 |
0.90000 |
0.92600 |
| 342.50 |
0.93500 |
0.95000 |
| 342.20 |
0.96900 |
0.97600 |
| 341.95 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Myers H.S.: V-L Equilibrium for Naphthenes and Paraffins. Petrol.Refiner 36 (1957) 175-178 |
Diagrams
List of All References
| Source |
| Susarev M.P.; Chen S.T.: The Benzene-n-Hexane-Cyclo-Hexane System. Russ.J.Phys.Chem. 37 (1963) 938-943 |
| Ridgway K.; Butler P.A.: Some Physical Properties of the Ternary System Benzene-Cyclohexane-n-Hexane. J.Chem.Eng.Data 12 (1967) 509-515 |
| Myers H.S.: V-L Equilibrium for Naphthenes and Paraffins. Petrol.Refiner 36 (1957) 175-178 |
Vapor-Liquid Equilibrium Data Overview
© DDBST GmbH
