SDS Volume

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

Source Publication

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

Conditions:

Room Temp: 298 $\pu{K}$

Compiler:

A. Skrzecz

Methodology:

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].

Sample Information:
  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 99.6 mole% by GLC; $d$ = 0.86032, $n$ = 1.54946.
  3. Source not specified.
Measurement 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.

Methodology Citations

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).

System Components:
  1. 2-Propanol, $\ce{ C3H8O }$; [67-63-0] NIST WebBook
  2. 1,3-Dimethylbenzene, $\ce{ C8H10 }$; [108-38-3] NIST WebBook
  3. Water, $\ce{ H2O }$; [7732-18-5] NIST WebBook
Experimental Data
$T$ (°C) $T$ ($\pu{K}$) w1 w2 $x_{1}$ $x_{2}$
25.0298.2 0.00.0000.0000.000
25.0298.2 0.2495 x 10-30.0911 x 10-3
25.0298.2 0.3479 x 10-30.1392 x 10-3
25.0298.2 0.4320.0390.1950.010
25.0298.2 0.4980.0940.2610.028
25.0298.2 0.5030.2150.3220.078
25.0298.2 0.4820.3230.3670.139
25.0298.2 0.4360.4350.3910.221
25.0298.2 0.3690.5520.3900.330
25.0298.2 0.2870.6690.3530.466
25.0298.2 0.1960.7830.2760.625
25.0298.2 0.0990.8940.1570.806
25.0298.2 0.0510.9460.0850.899
25.0298.2 0.00.9990.0000.997

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