SDS Volume
Volume 69. Ternary Alcohol-Hydrocarbon-Water Systems, p None
Source Publication
Kogan, V. B.; Deizenrot, I. V.; Kulbyaeva, T. A.; Fridman, V. M.; Zh. Prikl. Khim. 29, 1387 (1956).
Conditions:
Room Temp: 283 - 293 $\pu{K}$
Compiler:
Methodology:
The analytical method was used. The two phase mixture was periodically shaken in a thermostated burette with water jacket for several hours. The phases were removed for analysis after separation. Methanol was determined by the Karl Fischer method. Water concentration in hydrocarbon-rich phase was smaller then 0.001-0.02%.
Sample Information:
- Source not specified, pure grade; distilled; contained <0.01% of water; $n^{20}$ = 1.3391.
- Source not specified; used as received; BP = 98.4°C, $n^{20}$ = 1.3877.
- Source not specified.
Measurement Errors:
Ambient temperature: Temp. ±0.05°C; soly. < ±1% (relative error of methanol concentration).
Mass concentration (m/v) (1): Not reported.
System Components:
- Methanol, $\ce{ CH4O }$; [67-56-1] NIST WebBook
- Heptane, $\ce{ C7H16 }$; [142-82-5] NIST WebBook
- Water, $\ce{ H2O }$; [7732-18-5] NIST WebBook
Experimental Data
| $T$ (°C) | $T$ ($\pu{K}$) | w1 | w2 | $x_{1}$ | $x_{2}$ |
|---|---|---|---|---|---|
| 20.0 | 293.15 | 0.066 | 0.934 | 0.1810 | 0.8190 |
| 10.0 | 283.15 | 0.038 | 0.962 | 0.1099 | 0.8901 |
| 10.0 | 283.2 | 8 x 10-3 | 0.992 | 0.0246 | 0.9754 |
| 20.0 | 293.15 | 0.020 | 0.980 | 0.0600 | 0.9400 |
| 20.0 | 293.15 | 0.011 | 0.989 | 0.0336 | 0.9664 |
| 10.0 | 283.2 | 4 x 10-3 | 0.996 | 0.0124 | 0.9876 |
| 10.0 | 283.2 | 3 x 10-3 | 0.997 | 9.3 x 10-3 | 0.9907 |
| 20.0 | 293.15 | 2.1 x 10-3 | 0.9979 | 6.5 x 10-3 | 0.9935 |
| 20.0 | 293.15 | 0.777 | 0.233 | 0.9159 | 0.0841 |
| 10.0 | 283.2 | 0.790 | 0.210 | 0.9217 | 0.0783 |
| 20.0 | 293.15 | 0.860 | 0.0973 | 0.8893 | 0.0322 |
| 10.0 | 283.2 | 0.867 | 0.0565 | 0.8491 | 0.0177 |
| 10.0 | 283.2 | 0.844 | 0.018 | 0.7706 | 5.3 x 10-3 |
| 20.0 | 293.15 | 0.860 | 0.032 | 0.8095 | 9.6 x 10-3 |
| 10.0 | 283.2 | 0.799 | 9 x 10-3 | 0.6988 | 2.5 x 10-3 |
| 20.0 | 293.15 | 0.781 | 0.000 | 0.6672 | 0.0000 |


