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 305
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
| 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] |
| 394.90 |
0.10900 |
0.21700 |
| 393.25 |
0.20800 |
0.33200 |
| 392.25 |
0.29500 |
0.41300 |
| 391.55 |
0.36100 |
0.46500 |
| 390.95 |
0.43300 |
0.51700 |
| 390.65 |
0.44700 |
0.52900 |
| 390.45 |
0.51000 |
0.56900 |
| 390.25 |
0.54400 |
0.60100 |
| 389.95 |
0.55400 |
0.60700 |
| 389.75 |
0.57500 |
0.61900 |
| 389.55 |
0.60800 |
0.64200 |
| 389.45 |
0.64600 |
0.66900 |
| 389.35 |
0.67900 |
0.69200 |
| 389.35 |
0.71000 |
0.71500 |
| 389.75 |
0.72600 |
0.73400 |
| 389.35 |
0.72900 |
0.72900 |
| 389.70 |
0.73100 |
0.73300 |
| 389.70 |
0.75600 |
0.75000 |
| 389.45 |
0.82800 |
0.81300 |
| 389.95 |
0.86500 |
0.85000 |
| 390.15 |
0.91300 |
0.89500 |
| 390.15 |
0.96000 |
0.94200 |
| 390.15 |
0.98000 |
0.96400 |
| 390.15 |
0.99500 |
0.98900 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Brunjes A.S.; Furnas C.C.: Vapor-Liquid Equilibrium Data for Commercially Important Systems of Organic Solvents. Ind.Eng.Chem. Ind.Ed. 27 (1935) 396-400 |
Vapor-Liquid Equilibrium Data Set 4145
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
| 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] |
| 325.75 |
0.00000 |
0.00000 |
| 324.65 |
0.18000 |
0.22500 |
| 324.25 |
0.28200 |
0.32200 |
| 323.95 |
0.35500 |
0.36300 |
| 323.85 |
0.37000 |
0.37000 |
| 323.95 |
0.43500 |
0.41600 |
| 324.05 |
0.48700 |
0.43700 |
| 324.35 |
0.59100 |
0.50400 |
| 325.45 |
0.76500 |
0.64500 |
| 326.65 |
0.86800 |
0.75200 |
| 327.85 |
0.92100 |
0.83300 |
| 329.25 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Sheinker Yu.N.; Peresleni E.M.: Dampf-Flüssig-Gleichgewicht in einigen binären Systemen bei niedrigen Drücken. Zh.Fiz.Khim. 26 (1952) 1103-1109 |
Vapor-Liquid Equilibrium Data Set 4146
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
| 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] |
| 353.65 |
0.00000 |
0.00000 |
| 351.35 |
0.16100 |
0.21000 |
| 350.05 |
0.31300 |
0.37500 |
| 349.55 |
0.47400 |
0.47900 |
| 349.65 |
0.61300 |
0.57800 |
| 349.95 |
0.67500 |
0.62000 |
| 350.35 |
0.77700 |
0.70500 |
| 351.45 |
0.87300 |
0.80700 |
| 353.45 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Sheinker Yu.N.; Peresleni E.M.: Dampf-Flüssig-Gleichgewicht in einigen binären Systemen bei niedrigen Drücken. Zh.Fiz.Khim. 26 (1952) 1103-1109 |
Diagrams
List of All References
| Source |
| Sheinker Yu.N.; Peresleni E.M.: Dampf-Flüssig-Gleichgewicht in einigen binären Systemen bei niedrigen Drücken. Zh.Fiz.Khim. 26 (1952) 1103-1109 |
| Brunjes A.S.; Furnas C.C.: Vapor-Liquid Equilibrium Data for Commercially Important Systems of Organic Solvents. Ind.Eng.Chem. Ind.Ed. 27 (1935) 396-400 |
Vapor-Liquid Equilibrium Data Overview
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