Glenn T. Hefter 1 1.5e+01 Ambient temperature 2 1.5 °C -1 6.53e-01 Relative mass - solution (1) 3 6.53 mg/kg 1 -7 1.03e-07 Mole fraction - Liquid (1) 3 1.03 1 -5 6.53e-05 Relative mass - solution (1) 3 6.53 g₁/100 g sln 1 2.0e+01 Ambient temperature 2 2.0 °C -1 6.28e-01 Relative mass - solution (1) 3 6.28 mg/kg 2 -8 9.9e-08 Mole fraction - Liquid (1) 2 9.9 1 -5 6.28e-05 Relative mass - solution (1) 3 6.28 g₁/100 g sln 1 2.5e+01 Ambient temperature 2 2.5 °C -1 6.15e-01 Relative mass - solution (1) 3 6.15 mg/kg 3 -8 9.7e-08 Mole fraction - Liquid (1) 2 9.7 1 -5 6.15e-05 Relative mass - solution (1) 3 6.15 g₁/100 g sln 1 3.0e+01 Ambient temperature 2 3.0 °C -1 6.12e-01 Relative mass - solution (1) 3 6.12 mg/kg 4 -8 9.6e-08 Mole fraction - Liquid (1) 2 9.6 1 -5 6.12e-05 Relative mass - solution (1) 3 6.12 g₁/100 g sln 1 3.5e+01 Ambient temperature 2 3.5 °C -1 6.20e-01 Relative mass - solution (1) 3 6.20 mg/kg 5 -8 9.8e-08 Mole fraction - Liquid (1) 2 9.8 1 -5 6.20e-05 Relative mass - solution (1) 3 6.20 g₁/100 g sln 1 Solubility, Solubility data series 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]. The International Union of Pure and Applied Chemistry Vejrosta, J.; Novak, J.; Jonsson, J. A.; Fluid Phase Equil. 1982, 8, 25-35. paper https://doi.org/10.1016/0378-3812(82)80003-4 Jonsson, J. A.; Vejrosta, J.; Novak, J.; Fluid Phase Equilib. 1982, 9, 279-86. paper https://doi.org/10.1016/0378-3812(82)80023-x 111-65-9 1 C8H18 InChI=1S/C8H18/c1-3-5-7-8-6-4-2/h3-8H2,1-2H3 TVMXDCGIABBOFY-UHFFFAOYSA-N 114.229 Octane Fluka, >99.8%, used as received. 7732-18-5 2 H2O InChI=1S/H2O/h1H2 XLYOFNOQVPJJNP-UHFFFAOYSA-N 18.0153 Water not specified. Octane with Water