SDS Volume (658)

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

Original Measurements

Jonsson, J. A.; Vejrosta, J.; Novak, J.; Fluid Phase Equilib. 1982, 9, 279-86.

Variables:

Room Temp: 15 -35 °C

Prepared by:

G.T. Hefter

Method/Apparatus/Procedure:

Air-water partition coefficients were measured by saturating a portion of water by a stream of nitrogen containing a known vapour concentration of (1). After equilibration, the dissolved (1) was adsorbed in a porous polymer trap and the entrapped (1) analyzed by gas chromatography. The method and apparatus are described in detail in [1].

Source and Purity of Materials:
  1. Fluka, >99.8%, used as received.
  2. not specified.
Estimated Errors:

Ambient temperature: Not specified.

References

1 Vejrosta, J.; Novak, J.; Jonsson, J. A.; Fluid Phase Equil. 1982, 8, 25-35.

Components:
  1. Octane, $\ce{ C8H18 }$; [111-65-9] NIST WebBook
  2. Water, $\ce{ H2O }$; [7732-18-5] NIST WebBook
Experimental Data

Solubility values were calculated by the authors from their smoothed air-water partition coefficient (KAW) by assuming KAW values obtained at infinite dilution were valid at the saturatioin pressure of (1).

Solubility of octane in water
$T$ (°C) MR1 (mg/kg) $x_{1}$ MR1 (g1/100 g sln)
15 0.653 1.03 x 10-76.53 x 10-5
20 0.628 9.9 x 10-86.28 x 10-5
25 0.615 9.7 x 10-86.15 x 10-5
30 0.612 9.6 x 10-86.12 x 10-5
35 0.620 9.8 x 10-86.20 x 10-5

(a) These values were calculated by the compiler.

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