SDS Volume (3737)

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

Original Measurements

Letcher, T. M.; Siswana, P. M.; Fluid Phase Equilib. 74, 203 (1992).

Variables:

Room Temp: 298 $\pu{K}$

Prepared by:

A. Skrzecz

Method/Apparatus/Procedure:

The points on the binodal curve were determined by the formation of a cloudy mixture on shaking after the addition of a known mass of one component to a mixture of known masses of the other two components. Precision weighing syringes were used as described in [1]. Tie line compositions were determined by the refractive index method reported in [2] and complementary method using the Karl Fischer titrations as reported in [3].

Source and Purity of Materials:
  1. Merck, AR grade; refluxed with $\ce{Mg}$ and $\ce{I2}$, distilled; purity $\pu{\gt 99.6 mole%}$ by GLC; $d$ = 0.78151, $n$ = 1.3752.
  2. BDH; used as received; purity better than $\pu{99.6 mole%}$ by GLC.
  3. Source not specified.
Estimated Errors:

Ambient temperature: Estimated comp. 0.005 mole fraction on the binodal curve and 0.01 mole fraction for tie lines (estimated by the authors).
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. Toluene, $\ce{ C7H8 }$; [108-88-3] 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 0.0911 x 10-3 0.2494 x 10-3
25.0298.2 0.1385 x 10-3 0.3430.019
25.0298.2 0.1930.019 0.4210.064
25.0298.2 0.2550.049 0.4730.139
25.0298.2 0.2980.083 0.4880.208
25.0298.2 0.3530.154 0.4790.320
25.0298.2 0.3780.247 0.4350.436
25.0298.2 0.3710.362 0.3690.552
25.0298.2 0.3290.500 0.2870.668
25.0298.2 0.2520.656 0.1960.782
25.0298.2 0.1420.834 0.0990.896
25.0298.2 0.0730.918 0.0490.949
25.0298.2 0.0000.999 0.00.9998

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