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 by the refractive index method reported in [2] and a complementary method using the Karl Fischer titrations as reported in [3].

Sample Information:
  1. Merck, AR grade; distilled, dried by the addition of anhydrous potassium carbonate, distilled; purity better than $\pu{99.6 mole%}$ by GLC.
  2. BDH; used as received; purity better than $\pu{99.6 mole%}$ by GLC.
  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-Butanol, $\ce{ C4H10O }$; [78-92-2] NIST WebBook
  2. 1,3,5-Trimethylbenzene, $\ce{ C9H12 }$; [108-67-8] NIST WebBook
  3. Water, $\ce{ H2O }$; [7732-18-5] NIST WebBook
Experimental Data
$T$ (°C) $T$ ($\pu{K}$) $x_{1}$ $x_{2}$ w1 w2
25.0298.2 0.0000.000 0.00.000
25.0298.2 0.0510.000 0.1810.000
25.0298.2 0.3120.000 0.6510.000
25.0298.2 0.3920.018 0.6940.052
25.0298.2 0.4350.033 0.7040.087
25.0298.2 0.4820.074 0.6790.169
25.0298.2 0.5040.134 0.6230.268
25.0298.2 0.5050.208 0.5540.370
25.0298.2 0.4790.295 0.4730.473
25.0298.2 0.4310.399 0.3850.578
25.0298.2 0.3690.520 0.2980.680
25.0298.2 0.2690.663 0.1980.790
25.0298.2 0.1420.828 0.0950.900
25.0298.2 0.0770.913 0.0490.949
25.0298.2 0.0000.999 0.00.9998

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