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 9531
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
| 4 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
x3 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
y3 [mol/mol] |
| 353.76 |
0.10175 |
0.17201 |
0.05445 |
0.23341 |
0.35596 |
0.04027 |
| 351.48 |
0.04271 |
0.65325 |
0.02279 |
0.06071 |
0.71710 |
0.00413 |
| 350.91 |
0.21580 |
0.15039 |
0.04764 |
0.46206 |
0.21825 |
0.02317 |
| 350.52 |
0.09753 |
0.61618 |
0.02146 |
0.13494 |
0.65233 |
0.00394 |
| 345.09 |
0.41083 |
0.28249 |
0.02292 |
0.59974 |
0.24625 |
0.00408 |
| 340.95 |
0.74198 |
0.02290 |
0.01764 |
0.90764 |
0.01337 |
0.00249 |
| 342.24 |
0.62232 |
0.18220 |
0.01482 |
0.81143 |
0.10383 |
0.00214 |
| 352.48 |
0.10927 |
0.38029 |
0.14486 |
0.19682 |
0.45580 |
0.03677 |
| 348.85 |
0.04697 |
0.73367 |
0.06230 |
0.08169 |
0.75696 |
0.00660 |
| 349.72 |
0.17630 |
0.48529 |
0.09619 |
0.27832 |
0.51078 |
0.01671 |
| 343.05 |
0.64046 |
0.04635 |
0.08840 |
0.85309 |
0.02793 |
0.01101 |
| 344.47 |
0.45791 |
0.31846 |
0.06304 |
0.66505 |
0.22609 |
0.00629 |
| 340.45 |
0.77996 |
0.05864 |
0.04612 |
0.92077 |
0.02934 |
0.00493 |
| 343.08 |
0.52571 |
0.36561 |
0.03107 |
0.66759 |
0.26511 |
0.00321 |
| 352.87 |
0.21383 |
0.14871 |
0.39967 |
0.41995 |
0.18225 |
0.08233 |
| 351.15 |
0.09354 |
0.62762 |
0.17505 |
0.16417 |
0.68648 |
0.02476 |
| 347.19 |
0.39878 |
0.11341 |
0.30507 |
0.71535 |
0.10531 |
0.04379 |
| 349.03 |
0.20165 |
0.55420 |
0.15439 |
0.31727 |
0.56435 |
0.01424 |
| 342.85 |
0.67333 |
0.11846 |
0.13060 |
0.87068 |
0.07857 |
0.01389 |
| 351.05 |
0.09141 |
0.63554 |
0.19686 |
0.15748 |
0.74383 |
0.01702 |
| 346.69 |
0.37279 |
0.25926 |
0.31450 |
0.70456 |
0.21946 |
0.02667 |
| 360.85 |
0.06319 |
0.04395 |
0.40084 |
0.16845 |
0.11064 |
0.13270 |
| 360.28 |
0.04920 |
0.07213 |
0.25070 |
0.14723 |
0.16321 |
0.12472 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Karaseva A.P.; Frolov A.F.; Loginova M.A.: Flüssigkeits-Dampf-Gleichgewicht im System Methanol-Äthanol-n-Butanol-Wasser. Izv.Vyssh.Uchebn.Zaved.Khim.Khim.Tekhnol. 12 (1969) 1661-1665 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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