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 8906
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
| 2 |
H2O |
18.015 |
7732-18-5 |
Water |
| 3 |
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] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 378.15 |
0.72000 |
0.10000 |
0.39800 |
0.47100 |
| 371.30 |
0.64000 |
0.20000 |
0.30700 |
0.58200 |
| 365.50 |
0.48000 |
0.40000 |
0.20000 |
0.70800 |
| 364.28 |
0.32000 |
0.60000 |
0.18600 |
0.72300 |
| 364.28 |
0.15900 |
0.80100 |
0.18300 |
0.72300 |
| 377.35 |
0.53900 |
0.10100 |
0.31300 |
0.46100 |
| 369.95 |
0.48000 |
0.20000 |
0.23200 |
0.58000 |
| 364.05 |
0.36000 |
0.40000 |
0.14500 |
0.71200 |
| 364.05 |
0.24000 |
0.60000 |
0.14300 |
0.71200 |
| 364.05 |
0.12000 |
0.80000 |
0.14200 |
0.71400 |
| 375.45 |
0.36000 |
0.10000 |
0.22400 |
0.51600 |
| 368.25 |
0.32200 |
0.20000 |
0.16300 |
0.60100 |
| 363.60 |
0.24000 |
0.40000 |
0.10300 |
0.70700 |
| 363.60 |
0.16200 |
0.60600 |
0.10300 |
0.70800 |
| 363.60 |
0.08000 |
0.80000 |
0.10300 |
0.70700 |
| 375.69 |
0.18000 |
0.10000 |
0.14600 |
0.50200 |
| 369.01 |
0.16000 |
0.20100 |
0.08600 |
0.65400 |
| 363.55 |
0.11900 |
0.39800 |
0.06200 |
0.70800 |
| 363.55 |
0.08000 |
0.60000 |
0.06400 |
0.70100 |
| 363.55 |
0.04000 |
0.80000 |
0.06400 |
0.70300 |
| 363.53 |
0.07260 |
0.70340 |
0.07260 |
0.70340 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Beregovykh V.V.; Timofeev V.S.; Lukyanova R.N.; Yakushev V.M.; Serafimov L.A.: Die Phasengleichgewichte in den Systemen n-Propanol-Wasser-n-Butylacetat und n-Butanol-Wasser-n-Butylacetat bei Atmosphärendruck. Uch.Zap.Mosk.Inst.Tonkoj Khim.Tekhnol. 1 (1971) 31-38 |
Vapor-Liquid Equilibrium Data Set 21057
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
H2O |
18.015 |
7732-18-5 |
Water |
| 2 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
| 3 |
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] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 363.45 |
0.99400 |
0.00500 |
0.70900 |
0.07290 |
| 363.75 |
0.99300 |
0.00680 |
0.71200 |
0.10900 |
| 364.00 |
0.98900 |
0.01010 |
0.71100 |
0.14900 |
| 364.15 |
0.98900 |
0.01070 |
0.72300 |
0.16100 |
| 364.40 |
0.98800 |
0.01190 |
0.72700 |
0.18300 |
| 365.10 |
0.98600 |
0.01380 |
0.74100 |
0.20900 |
| 363.45 |
0.19900 |
0.17900 |
0.70900 |
0.07290 |
| 363.75 |
0.30900 |
0.31200 |
0.71200 |
0.10900 |
| 364.00 |
0.40100 |
0.37000 |
0.71100 |
0.14900 |
| 364.15 |
0.45000 |
0.38800 |
0.72300 |
0.16100 |
| 364.40 |
0.47900 |
0.40400 |
0.72700 |
0.18300 |
| 365.10 |
0.55600 |
0.39400 |
0.74100 |
0.20900 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Gomis V.; Ruiz F.; Asensi J.C.: The Application of Ultrasound in the Determination of Isobaric Vapour-Liquid-Liquid Equilibrium Data. Fluid Phase Equilib. 172 (2000) 245-259 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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