SDS Volume (4463)
Volume 72. Nitromethane with Water or Organic Solvents: Ternary and Quaternary Systems, p None
Original Measurements
Lakshmanan, C. M.; Laddha, G. S.; J. Am. Oil Chem. Soc. 37, 466-8 (1960).
Variables:
Room Temp: 303 $\pu{K}$
Prepared by:
Method/Apparatus/Procedure:
The method of Treybal [1] was used. For determining the phase distribution data, known mixtures of ternary constituents comprising of (1), (2) and (3) well within the heterogeneous region were placed in a constant temperature bath after vigorous agitation and allowed to separate into two phases after attaining equilibrium. The two phases were separated and weighed. A weighed quantity of each phase was taken in a distilling flask, and water bath. Traces of (1) and (2) remaining were removed under vacuum by drying the esters on a water bath to constant weight under a stream of carbon dioxide. Total weight of the esters thus obtained was checked against the weight of ester taken originally in the mixture.
Source and Purity of Materials:
- Fluka AG; distilled; BP = 100.5-101.5°C, $n_{D}^{30}$, = 1.3770, $d_{4}^{30}$ = 1.1237.
- BDH Ltd.; laboratory reagent-grade; distilled; BP = 67-70°C, $n_{D}^{30}$, = 1.3761, $d_{4}^{30}$ = 0.6782.
- Prepared by methylation of castor oil; using $\ce{HCl}$ as catalyst; dried and distilled.
Estimated Errors:
Ambient temperature: control to ±0.1 K.
References
1 Treybal, R. E.; Liquid Extraction, McGraw-Hill, New York, 1951.
Components:
- Nitromethane, $\ce{ CH3NO2 }$; [75-52-5] NIST WebBook
- Hexane, $\ce{ C6H14 }$; [110-54-3] NIST WebBook
- Castor oil methyl esters, [68201-34-3] NIST WebBook
Experimental Data
Estimated plait point: w1 = 0.649, w2 = 0.109, and w3 = 0.242.
Table 2. Equilibrium tie lines data for the ternary system
| $T$ (°C) | $T$ ($\pu{K}$) | w3 |
|---|---|---|
| 30.0 | 303.2 | 0.0368 |
| 30.0 | 303.2 | 0.0572 |
| 30.0 | 303.2 | 0.0605 |
| 30.0 | 303.2 | 0.0679 |
| 30.0 | 303.2 | 0.0786 |
| 30.0 | 303.2 | 0.0831 |
| 30.0 | 303.2 | 0.0821 |
| 30.0 | 303.2 | 0.0975 |
| 30.0 | 303.2 | 0.1064 |
| 30.0 | 303.2 | 0.1077 |
| 30.0 | 303.2 | 0.1227 |
| 30.0 | 303.2 | 0.1314 |
| 30.0 | 303.2 | 0.1411 |
| 30.0 | 303.2 | 0.1901 |
| 30.0 | 303.2 | 0.0753 |
| 30.0 | 303.2 | 0.1588 |
| 30.0 | 303.2 | 0.1565 |
| 30.0 | 303.2 | 0.1520 |
| 30.0 | 303.2 | 0.2818 |
| 30.0 | 303.2 | 0.2795 |
| 30.0 | 303.2 | 0.2766 |
| 30.0 | 303.2 | 0.3684 |
| 30.0 | 303.2 | 0.3656 |
| 30.0 | 303.2 | 0.3616 |
| 30.0 | 303.2 | 0.3905 |
| 30.0 | 303.2 | 0.3841 |
| 30.0 | 303.2 | 0.3794 |
| 30.0 | 303.2 | 0.3635 |
(*) This table was prepared by the compiler from the published curve of ternary system solubility.


