Glenn T. Hefter 1 1.5e+01 Ambient temperature 2 1.5 °C 1 4.29e+01 Relative mass - solution (1) 3 4.29 mg/kg 1 -5 1.07e-05 Mole fraction - Liquid (1) 3 1.07 1 -3 4.29e-03 Relative mass - solution (1) 3 4.29 g₁/100 g sln 1 2.0e+01 Ambient temperature 2 2.0 °C 1 4.14e+01 Relative mass - solution (1) 3 4.14 mg/kg 2 -5 1.03e-05 Mole fraction - Liquid (1) 3 1.03 1 -3 4.14e-03 Relative mass - solution (1) 3 4.14 g₁/100 g sln 1 2.5e+01 Ambient temperature 2 2.5 °C 1 4.06e+01 Relative mass - solution (1) 3 4.06 mg/kg 3 -5 1.01e-05 Mole fraction - Liquid (1) 3 1.01 1 -3 4.06e-03 Relative mass - solution (1) 3 4.06 g₁/100 g sln 1 3.0e+01 Ambient temperature 2 3.0 °C 1 4.03e+01 Relative mass - solution (1) 3 4.03 mg/kg 4 -5 1.01e-05 Mole fraction - Liquid (1) 3 1.01 1 -3 4.03e-03 Relative mass - solution (1) 3 4.03 g₁/100 g sln 1 3.5e+01 Ambient temperature 2 3.5 °C 1 4.06e+01 Relative mass - solution (1) 3 4.06 mg/kg 5 -5 1.01e-05 Mole fraction - Liquid (1) 3 1.01 1 -3 4.06e-03 Relative mass - solution (1) 3 4.06 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 109-66-0 1 C5H12 InChI=1S/C5H12/c1-3-5-4-2/h3-5H2,1-2H3 OFBQJSOFQDEBGM-UHFFFAOYSA-N 72.1488 Pentane Fluka, >99.8%, used as received. 7732-18-5 2 H2O InChI=1S/H2O/h1H2 XLYOFNOQVPJJNP-UHFFFAOYSA-N 18.0153 Water Not specified. Pentane with Water