SDS Volume

Volume 38. Hydrocarbons in Water and Seawater, Part II, p None

Source Publication

Sanemasa, I.; Araki, M.; Deguchi, T.; Nagai, H.; Chem. Lett. 1981, 225-8.

Conditions:

Room Temp: 15 - 45 °C

Compiler:

M.C. Haulait-Pirson

Methodology:

The apparatus used for attaining solubility equilibrium is described in detail in the paper. Liquid (1) and redistilled (2) were placed in a vessel and a thermostatted funnel respectively. The solute vapor, generated by bubbling air through the liquid solute was introduced into the funnel and circulated by means of a pump. The circulation rate was 2 L/min. Solubility equilibria were attained within 5 min. Then portions of 10 mL of the aqueous sln were transferred into funnels to which 10 mL of chloroform had been added. Experimental procedures involved in spectrophotometric measuring the chloroform extracts were not reported. The solubility runs were made such that the temperature of solute reservoir was made to vary while that of solvent phase was held constant. The soubility obeys Henry's law at constant solvent temperature. Solubility values were calculated from Henry's law constants.

Sample Information:
  1. Analytical reagent grade used as purchased.
  2. redistilled.
Measurement Errors:

Mass concentration (m/v) (1): given above

System Components:
  1. 1,3,5-Trimethylbenzene, $\ce{ C9H12 }$; [108-67-8] NIST WebBook
  2. Water, $\ce{ H2O }$; [7732-18-5] NIST WebBook
Experimental Data
$T$ (°C) $x_{1}$ MR1 (g1/100 g2)
15 6.82 x 10-6a4.56 x 10-3
25 7.41 x 10-6a4.95 x 10-3
35 8.11 x 10-6a5.42 x 10-3
45 8.46 x 10-6a5.65 x 10-3

(a) Calculated by compiler assuming a solution density of 1.00 g mL-1.

Download Data   link to XML output link to JSON output link to JSON-LD output