SDS Volume

Volume 72. Nitromethane with Water or Organic Solvents: Ternary and Quaternary Systems, p 1604

Source Publication

Lakshmanan, C. M.; Laddha, G. S.; J. Am. Oil Chem. Soc. 37, 466-8 (1960).

Conditions:

Room Temp: 303 $\pu{K}$

Compiler:

V.P. Sazonov

Methodology:

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.

Sample Information:
  1. Fluka AG; distilled; BP = 100.5-101.5°C, $n_{D}^{30}$, = 1.3770, $d_{4}^{30}$ = 1.1237.
  2. BDH Ltd.; laboratory reagent-grade; distilled; BP = 67-70°C, $n_{D}^{30}$, = 1.3761, $d_{4}^{30}$ = 0.6782.
  3. Prepared by methylation of castor oil; using $\ce{HCl}$ as catalyst; dried and distilled.
Measurement Errors:

Ambient temperature: control to ±0.1 K.

Methodology Citation

1 Treybal, R. E.; Liquid Extraction, McGraw-Hill, New York, 1951.

System Components:
  1. Nitromethane, $\ce{ CH3NO2 }$; [75-52-5] NIST WebBook
  2. Hexane, $\ce{ C6H14 }$; [110-54-3] NIST WebBook
  3. Castor oil methyl esters, [68201-34-3] NIST WebBook
Experimental Data

Estimated plait point: w1 = 0.649, w2 = 0.109, and w3 = 0.242.

$T$ (°C) $T$ ($\pu{K}$) w3
30.0303.2 0.0368
30.0303.2 0.0572
30.0303.2 0.0605
30.0303.2 0.0679
30.0303.2 0.0786
30.0303.2 0.0831
30.0303.2 0.0821
30.0303.2 0.0975
30.0303.2 0.1064
30.0303.2 0.1077
30.0303.2 0.1227
30.0303.2 0.1314
30.0303.2 0.1411
30.0303.2 0.1901
30.0303.2 0.0753
30.0303.2 0.1588
30.0303.2 0.1565
30.0303.2 0.1520
30.0303.2 0.2818
30.0303.2 0.2795
30.0303.2 0.2766
30.0303.2 0.3684
30.0303.2 0.3656
30.0303.2 0.3616
30.0303.2 0.3905
30.0303.2 0.3841
30.0303.2 0.3794
30.0303.2 0.3635

(*) This table was prepared by the compiler from the published curve of ternary system solubility.

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