SDS Volume
Volume 69. Ternary Alcohol-Hydrocarbon-Water Systems, p None
Source Publication
Sugi, H.; Katayama, T.; J. Chem. Eng. Jpn. 1977, 10, 400-2.
Conditions:
Room Temp: 298 $\pu{K}$
Compiler:
Methodology:
A combination of titration and analytical method was used. The apparatus and experimental procedure were described in [1]. For GLC analysis a 1.6 m column filled with Poropak-Q was used. Solubility of water in hexane was determined by the Karl Fischer method. Composition of the water-rich phase was determined by the gross composition of phase split liquid mixture and composition of the organic phase (concentration of hexane was assumed to be 0).
Sample Information:
- Merck Uvasol, spectrograde; used as received; densities agreed within 0.0003 with literature values.
- Merck Uvasol, spectrograde; used as received; densities agreed within 0.0003 with literature values.
- De-ionized, twice distilled.
Measurement Errors:
Ambient temperature: Not reported.
Mass concentration (m/v) (1): Not reported.
Methodology Citation
1 Sugi, H.; Nitta, T.; Katayama, T.; J. Chem. Eng. Jap. 1976, 9, 12.
System Components:
- 1-Butanol, $\ce{ C4H10O }$; [71-36-3] NIST WebBook
- Hexane, $\ce{ C6H14 }$; [110-54-3] NIST WebBook
- Water, $\ce{ H2O }$; [7732-18-5] NIST WebBook
Experimental Data
| $T$ (°C) | $T$ ($\pu{K}$) | $x_{1}$ | $x_{2}$ | w1 | w2 |
|---|---|---|---|---|---|
| 25.0 | 298.2 | 0.0000 | 0.99949 | 0.0 | 0.99989 |
| 25.0 | 298.2 | 0.1255 | 0.8630 | 0.1109 | 0.8866 |
| 25.0 | 298.2 | 0.1839 | 0.7960 | 0.1650 | 0.8306 |
| 25.0 | 298.2 | 0.2337 | 0.7342 | 0.2134 | 0.7795 |
| 25.0 | 298.2 | 0.2928 | 0.6459 | 0.2766 | 0.7093 |
| 25.0 | 298.2 | 0.3548 | 0.5557 | 0.3470 | 0.6318 |
| 25.0 | 298.2 | 0.4220 | 0.4460 | 0.4339 | 0.5331 |
| 25.0 | 298.2 | 0.4709 | 0.3427 | 0.5148 | 0.4356 |
| 25.0 | 298.2 | 0.5035 | 0.2714 | 0.5763 | 0.3611 |
| 25.0 | 298.2 | 0.5091 | 0.2560 | 0.5894 | 0.3446 |
| 25.0 | 298.2 | 0.5407 | 0.1598 | 0.6765 | 0.2324 |
| 25.0 | 298.2 | 0.5413 | 0.0792 | 0.7460 | 0.1269 |
| 25.0 | 298.2 | 0.5229 | 0.0310 | 0.7835 | 0.0540 |
| 25.0 | 298.2 | 0.5032 | 0.0000 | 0.8065 | 0.0000 |
| 25.0 | 298.2 | 0.0151 | 0.0000 | 0.0593 | 0.0000 |


