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 8904
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 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] |
| 357.60 |
0.10000 |
0.72000 |
0.33200 |
0.50400 |
| 355.75 |
0.20100 |
0.64000 |
0.40500 |
0.45600 |
| 353.96 |
0.41600 |
0.46800 |
0.47900 |
0.42400 |
| 352.55 |
0.60000 |
0.32000 |
0.64700 |
0.30200 |
| 351.84 |
0.79700 |
0.16200 |
0.84000 |
0.13700 |
| 358.65 |
0.10000 |
0.54000 |
0.28600 |
0.52500 |
| 356.55 |
0.20000 |
0.48000 |
0.36900 |
0.47300 |
| 354.46 |
0.40000 |
0.36000 |
0.44700 |
0.42900 |
| 353.05 |
0.60200 |
0.23900 |
0.64900 |
0.26600 |
| 352.18 |
0.79900 |
0.12050 |
0.81900 |
0.13800 |
| 359.65 |
0.09500 |
0.36150 |
0.25000 |
0.55100 |
| 357.29 |
0.20200 |
0.31900 |
0.38200 |
0.45600 |
| 355.36 |
0.40000 |
0.24000 |
0.51000 |
0.35200 |
| 353.86 |
0.60400 |
0.15700 |
0.67300 |
0.21300 |
| 352.66 |
0.80000 |
0.08000 |
0.83000 |
0.10000 |
| 363.00 |
0.10000 |
0.18000 |
0.19500 |
0.60200 |
| 360.37 |
0.20000 |
0.16000 |
0.39600 |
0.43600 |
| 357.45 |
0.40600 |
0.11900 |
0.60700 |
0.24200 |
| 355.25 |
0.60100 |
0.07950 |
0.74600 |
0.12500 |
| 353.24 |
0.80000 |
0.04000 |
0.84900 |
0.06400 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Beregovykh V.V.; Timofeev V.S.; Lukyanova R.N.; Serafimov L.A.: Die Phasengleichgewicht in den Systemen Methanol-Wasser-n-Butylacetat und Ethanol-Wasser- n-Butylacetat bei Atmosphärendruck. Uch.Zap.Mosk.Inst.Tonkoj Khim.Tekhnol. 1 (1971) 24-30 |
Vapor-Liquid Equilibrium Data Set 33550
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
H2O |
18.015 |
7732-18-5 |
Water |
| 2 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
| 3 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
| 324.65 |
0.44130 |
0.03160 |
| 324.75 |
0.43190 |
0.05220 |
| 325.00 |
0.40490 |
0.11160 |
| 325.30 |
0.38050 |
0.16500 |
| 325.55 |
0.36030 |
0.20940 |
| 325.65 |
0.34760 |
0.23720 |
| 325.85 |
0.33320 |
0.26870 |
| 326.30 |
0.29890 |
0.34400 |
| 326.55 |
0.27990 |
0.38590 |
| 326.85 |
0.25140 |
0.44830 |
| 327.65 |
0.20550 |
0.54900 |
| 328.40 |
0.17200 |
0.62270 |
| 330.00 |
0.12650 |
0.72230 |
| 331.65 |
0.09060 |
0.80130 |
| 323.80 |
0.24350 |
0.01780 |
| 323.85 |
0.23920 |
0.03540 |
| 324.15 |
0.22610 |
0.08790 |
| 324.55 |
0.20890 |
0.15760 |
| 324.60 |
0.20830 |
0.16000 |
| 324.85 |
0.19860 |
0.19910 |
| 325.35 |
0.18030 |
0.27290 |
| 325.45 |
0.17500 |
0.29430 |
| 325.90 |
0.15570 |
0.37210 |
| 326.35 |
0.14410 |
0.41890 |
| 327.20 |
0.12410 |
0.49940 |
| 327.55 |
0.11460 |
0.53780 |
| 328.75 |
0.08970 |
0.63810 |
| 330.25 |
0.06730 |
0.72850 |
| 333.95 |
0.04010 |
0.83840 |
| 341.95 |
0.01710 |
0.93120 |
| 323.70 |
0.10820 |
0.04070 |
| 323.90 |
0.10480 |
0.07070 |
| 324.00 |
0.10390 |
0.07920 |
| 324.15 |
0.10060 |
0.10820 |
| 324.55 |
0.09540 |
0.15450 |
| 325.00 |
0.08920 |
0.20910 |
| 325.15 |
0.08580 |
0.23950 |
| 325.30 |
0.08270 |
0.26740 |
| 325.95 |
0.07640 |
0.32300 |
| 326.10 |
0.07350 |
0.34880 |
| 326.35 |
0.06780 |
0.39880 |
| 327.65 |
0.05630 |
0.50110 |
(T - temperature, x - liquid mole fraction)
Reference
| Source |
| Li G.; Li Z.: Determination and Prediction of Vapor–Liquid Equilibria for a System Containing Water + Butyl Acetate + Cyclohexane + Ethanol. J.Chem.Eng.Data 57 (2012) 2543-2548 |
Vapor-Liquid Equilibrium Data Set 33551
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
H2O |
18.015 |
7732-18-5 |
Water |
| 2 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
| 3 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
| 339.65 |
0.44130 |
0.03160 |
| 339.75 |
0.43190 |
0.05220 |
| 340.15 |
0.40490 |
0.11160 |
| 340.50 |
0.38050 |
0.16500 |
| 340.75 |
0.36030 |
0.20940 |
| 340.95 |
0.34760 |
0.23720 |
| 341.15 |
0.33320 |
0.26870 |
| 341.65 |
0.29890 |
0.34400 |
| 342.00 |
0.27990 |
0.38590 |
| 342.40 |
0.25140 |
0.44830 |
| 343.25 |
0.20550 |
0.54900 |
| 344.15 |
0.17200 |
0.62270 |
| 346.00 |
0.12650 |
0.72230 |
| 348.05 |
0.09060 |
0.80130 |
| 338.75 |
0.24350 |
0.01780 |
| 338.85 |
0.23920 |
0.03540 |
| 339.20 |
0.22610 |
0.08790 |
| 339.70 |
0.20890 |
0.15760 |
| 339.75 |
0.20830 |
0.16000 |
| 340.00 |
0.19860 |
0.19910 |
| 340.55 |
0.18030 |
0.27290 |
| 340.75 |
0.17500 |
0.29430 |
| 341.35 |
0.15570 |
0.37210 |
| 342.05 |
0.14410 |
0.41890 |
| 342.95 |
0.12410 |
0.49940 |
| 343.35 |
0.11460 |
0.53780 |
| 344.75 |
0.08970 |
0.63810 |
| 346.55 |
0.06730 |
0.72850 |
| 351.55 |
0.04010 |
0.83840 |
| 360.75 |
0.01710 |
0.93120 |
| 338.65 |
0.10820 |
0.04070 |
| 338.95 |
0.10480 |
0.07070 |
| 339.05 |
0.10390 |
0.07920 |
| 339.25 |
0.10060 |
0.10820 |
| 339.65 |
0.09540 |
0.15450 |
| 340.15 |
0.08920 |
0.20910 |
| 340.50 |
0.08580 |
0.23950 |
| 340.75 |
0.08270 |
0.26740 |
| 341.25 |
0.07640 |
0.32300 |
| 341.55 |
0.07350 |
0.34880 |
| 342.05 |
0.06780 |
0.39880 |
| 343.35 |
0.05630 |
0.50110 |
(T - temperature, x - liquid mole fraction)
Reference
| Source |
| Li G.; Li Z.: Determination and Prediction of Vapor–Liquid Equilibria for a System Containing Water + Butyl Acetate + Cyclohexane + Ethanol. J.Chem.Eng.Data 57 (2012) 2543-2548 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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