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 4964
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
| 2 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 396.65 |
0.02300 |
0.10200 |
| 390.05 |
0.08500 |
0.30900 |
| 384.25 |
0.15200 |
0.46400 |
| 378.45 |
0.23700 |
0.60200 |
| 373.75 |
0.32300 |
0.68800 |
| 370.35 |
0.38300 |
0.74500 |
| 368.15 |
0.44100 |
0.77700 |
| 363.55 |
0.57800 |
0.84200 |
| 360.75 |
0.68700 |
0.88600 |
| 357.85 |
0.81000 |
0.92800 |
| 357.75 |
0.82600 |
0.93400 |
| 355.25 |
0.94300 |
0.97500 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Nagata I.: Vapor-Liquid Equilibrium Data for Binary Systems, Acetone-Methyl Acetate, Methyl Acetate-Carbon Tetrachloride, Benzene- Butyl Acetate and Cyclohexane-Butyl Actate. Mem.Fac.Technol.Kanazawa Univ. 3 (1964) 197-205 |
Vapor-Liquid Equilibrium Data Set 17251
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
| 2 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 9.895 |
0.00000 |
0.00000 |
| 16.136 |
0.07680 |
0.41490 |
| 21.793 |
0.16080 |
0.60520 |
| 22.120 |
0.16560 |
0.61370 |
| 27.694 |
0.25750 |
0.72110 |
| 30.656 |
0.31540 |
0.76520 |
| 35.834 |
0.42650 |
0.82350 |
| 40.423 |
0.53890 |
0.86400 |
| 44.454 |
0.65530 |
0.89790 |
| 48.055 |
0.76930 |
0.92760 |
| 51.316 |
0.87370 |
0.95650 |
| 53.644 |
0.95180 |
0.98100 |
| 54.727 |
0.98500 |
0.99300 |
| 55.195 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Wichterle I.; Linek J.: Isothermal vapor-liquid equilibria in binary mixtures of cyclohexane of methylcyclohexane with n-alkyl (ethyl, propyl, or butyl) ethanoates (acetates) at temperatures from 335 to 370 K. Eldata Int.Electron.J.Phys.-Chem.Data 2 (1996) 67-78 |
Vapor-Liquid Equilibrium Data Set 17252
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
| 2 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 18.940 |
0.00000 |
0.00000 |
| 29.071 |
0.08160 |
0.38900 |
| 38.358 |
0.17280 |
0.58250 |
| 47.283 |
0.27000 |
0.69880 |
| 50.968 |
0.31870 |
0.73330 |
| 59.336 |
0.43420 |
0.80360 |
| 66.892 |
0.54780 |
0.84880 |
| 73.289 |
0.66270 |
0.88660 |
| 78.923 |
0.77870 |
0.92070 |
| 83.810 |
0.87710 |
0.95160 |
| 87.662 |
0.95320 |
0.97950 |
| 89.330 |
0.98520 |
0.99230 |
| 89.990 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Wichterle I.; Linek J.: Isothermal vapor-liquid equilibria in binary mixtures of cyclohexane of methylcyclohexane with n-alkyl (ethyl, propyl, or butyl) ethanoates (acetates) at temperatures from 335 to 370 K. Eldata Int.Electron.J.Phys.-Chem.Data 2 (1996) 67-78 |
Diagrams
List of All References
| Source |
| Nagata I.: Vapor-Liquid Equilibrium Data for Binary Systems, Acetone-Methyl Acetate, Methyl Acetate-Carbon Tetrachloride, Benzene- Butyl Acetate and Cyclohexane-Butyl Actate. Mem.Fac.Technol.Kanazawa Univ. 3 (1964) 197-205 |
| Wichterle I.; Linek J.: Isothermal vapor-liquid equilibria in binary mixtures of cyclohexane of methylcyclohexane with n-alkyl (ethyl, propyl, or butyl) ethanoates (acetates) at temperatures from 335 to 370 K. Eldata Int.Electron.J.Phys.-Chem.Data 2 (1996) 67-78 |
Vapor-Liquid Equilibrium Data Overview
© DDBST GmbH
