SDS Volume (3727)

Volume 69. Ternary Alcohol-Hydrocarbon-Water Systems, p None

Original Measurements

Letcher, T. M.; Siswana, P.; Radloff, S. E.; S. Afr. J. Chem. 44, 118 (1991).

Variables:

Room Temp: 298 $\pu{K}$

Prepared by:

A. Skrzecz

Method/Apparatus/Procedure:

The points on the binodal curve were determined by the titration method, as described in [1]. The formation of a cloudy mixture was observed visually on shaking after addition of a known mass of the third component; syringes were precisely weighed. Tie line compositions were determined by the refractive index method [2], and a complementary method using the Karl Fischer titration [3]. Measurements were made at pressure of 94.7 kPa.

Source and Purity of Materials:
  1. Merck, AR grade; refluxed with $\ce{Mg}$ and $\ce{I2}$, distilled; purity $\pu{\gt 99.9 mole%}$ by GLC.
  2. BDH; Gold label grade; used as received; purity $\pu{\gt 99.9 mole%}$ by GLC.
  3. Source not specified.
Estimated Errors:

Ambient temperature: Composition ±0.005 mole fraction (binodal curve), ±0.01 mole fraction (tie lines).
Mass concentration (m/v) (1): Not reported.

References

1 Letcher, T. M.; Wootton, S.; Shuttleworth, B.; Heyward, C.; J. Chem. Thermodyn 18, 1037 (1986).
2 Briggs; S. W.; Comings, E. W.; Ind. Eng. Chem. 35, 411 (1943).
3 Letcher, T. M.; Siswana, P. M.; van der Watt, P.; Radloff, S.; J. Chem. Thermodyn. 21, 1053 (1989).

Components:
  1. 2-Propanol, $\ce{ C3H8O }$; [67-63-0] NIST WebBook
  2. Cyclohexane, $\ce{ C6H12 }$; [110-82-7] NIST WebBook
  3. Water, $\ce{ H2O }$; [7732-18-5] NIST WebBook
Experimental Data
Compositions along the saturation curve
$T$ (°C) $T$ ($\pu{K}$) $x_{1}$ $x_{2}$ w1 w2
25.0298.2 0.0000.000 0.00.000
25.0298.2 0.1404 x 10-3 0.3480.014
25.0298.2 0.1980.011 0.4390.034
25.0298.2 0.2750.026 0.5280.070
25.0298.2 0.3150.049 0.5490.119
25.0298.2 0.3650.096 0.5520.203
25.0298.2 0.3920.183 0.5050.330
25.0298.2 0.3940.280 0.4460.444
25.0298.2 0.3700.396 0.3720.558
25.0298.2 0.3200.534 0.2880.673
25.0298.2 0.2400.688 0.1960.786
25.0298.2 0.1310.846 0.0990.896
25.0298.2 0.0680.923 0.0500.948
25.0298.2 0.0000.999 0.00.9998

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