SDS Volume
Volume 69. Ternary Alcohol-Hydrocarbon-Water Systems, p None
Source Publication
Noda, K.; Sato, K.; Nagatsuka, K.; Ishida, K.; J. Chem. Eng. Jpn. 8, 492-3 (1975).
Conditions:
Room Temp: 273 - 293 $\pu{K}$
Compiler:
Methodology:
The analytical method was used, similar to that reported in [1]. Samples of each phase were analyzed by GLC on a 3 mm diameter by 3 m long column packed with Poropak R and using $\ce{H2}$ as a carrier gas. Each sample was injected several times and the composition was determined from chromatogram areas. Care was taken to avoid contamination by the surroundings, especially water vapor.
Sample Information:
- Source not specified, commercially available; guaranteed reagent; used as received.
- Takachiho Chemical Industry Co., Ltd; standard reagent; used as received.
- Distilled
Measurement Errors:
Ambient temperature: Not reported.
Mass concentration (m/v) (1): Not reported.
Methodology Citation
System Components:
- Methanol, $\ce{ CH4O }$; [67-56-1] NIST WebBook
- Butane, $\ce{ C4H10 }$; [106-97-8] NIST WebBook
- Water, $\ce{ H2O }$; [7732-18-5] NIST WebBook
Experimental Data
| $T$ (°C) | $T$ ($\pu{K}$) | w1 | w2 | w3 | $x_{1}$ | $x_{3}$ |
|---|---|---|---|---|---|---|
| 0.0 | 273.2 | 6 x 10-3 | 0.994 | 3 x 10-4 | 0.011 | 0.988 |
| 0.0 | 273.2 | 0.011 | 0.989 | 4 x 10-4 | 0.020 | 0.979 |
| 0.0 | 273.2 | 0.021 | 0.978 | 6 x 10-4 | 0.037 | 0.961 |
| 0.0 | 273.2 | 0.036 | 0.963 | 7 x 10-4 | 0.063 | 0.934 |
| 0.0 | 273.2 | 0.058 | 0.941 | 8 x 10-4 | 0.100 | 0.897 |
| 0.0 | 273.2 | 0.061 | 0.938 | 8 x 10-4 | 0.105 | 0.892 |
| 20.0 | 293.2 | 4 x 10-3 | 0.996 | 4 x 10-4 | 7 x 10-3 | 0.991 |
| 20.0 | 293.2 | 8 x 10-3 | 0.991 | 6 x 10-4 | 0.014 | 0.984 |
| 20.0 | 293.2 | 0.011 | 0.988 | 7 x 10-4 | 0.020 | 0.978 |
| 20.0 | 293.2 | 0.013 | 0.986 | 8 x 10-4 | 0.023 | 0.974 |
| 20.0 | 293.2 | 0.023 | 0.976 | 1 x 10-3 | 0.041 | 0.956 |
| 20.0 | 293.2 | 0.034 | 0.965 | 1 x 10-3 | 0.060 | 0.937 |
| 20.0 | 293.2 | 0.047 | 0.951 | 1.5 x 10-3 | 0.082 | 0.914 |
| 20.0 | 293.2 | 0.071 | 0.927 | 2 x 10-3 | 0.121 | 0.873 |


