Walter Hayduk 2 2.3815e+02 Ambient temperature 5 2.3815 $\pu{K}$ 1 -3.5e+01 Ambient temperature 2 -3.5 °C -2 1.41e-02 Mole fraction - Liquid (1) 3 1.41 1 2 1.5e+02 Solubility (Pressure per concentration) 2 1.5 $\pu{kPa}$ 0 5.5e+00 Solubility 2 5.5 $\pu{cm3(g) cm-3(s) cmHg-1}$ 2 1.046e+02 Henry's Law Solubility Coefficient 4 1.046 $\pu{atm-1}$ 1 2 2.3815e+02 Ambient temperature 5 2.3815 $\pu{K}$ 1 -3.5e+01 Ambient temperature 2 -3.5 °C -2 3.00e-02 Mole fraction - Liquid (1) 3 3.00 1 2 2.01e+02 Solubility (Pressure per concentration) 3 2.01 $\pu{kPa}$ 1 1.18e+01 Solubility 3 1.18 $\pu{cm3(g) cm-3(s) cmHg-1}$ 1 6.65e+01 Henry's Law Solubility Coefficient 3 6.65 $\pu{atm-1}$ 2 2 2.3815e+02 Ambient temperature 5 2.3815 $\pu{K}$ 1 -3.5e+01 Ambient temperature 2 -3.5 °C -2 6.04e-02 Mole fraction - Liquid (1) 3 6.04 1 2 3.02e+02 Solubility (Pressure per concentration) 3 3.02 $\pu{kPa}$ 1 2.48e+01 Solubility 3 2.48 $\pu{cm3(g) cm-3(s) cmHg-1}$ 1 4.92e+01 Henry's Law Solubility Coefficient 3 4.92 $\pu{atm-1}$ 3 2 2.3815e+02 Ambient temperature 5 2.3815 $\pu{K}$ 1 -3.5e+01 Ambient temperature 2 -3.5 °C -1 1.311e-01 Mole fraction - Liquid (1) 4 1.311 1 2 5.04e+02 Solubility (Pressure per concentration) 3 5.04 $\pu{kPa}$ 1 5.83e+01 Solubility 3 5.83 $\pu{cm3(g) cm-3(s) cmHg-1}$ 1 3.78e+01 Henry's Law Solubility Coefficient 3 3.78 $\pu{atm-1}$ 4 2 2.4815e+02 Ambient temperature 5 2.4815 $\pu{K}$ 1 -2.5e+01 Ambient temperature 2 -2.5 °C -2 1.08e-02 Mole fraction - Liquid (1) 3 1.08 1 2 1.5e+02 Solubility (Pressure per concentration) 2 1.5 $\pu{kPa}$ 0 4.2e+00 Solubility 2 4.2 $\pu{cm3(g) cm-3(s) cmHg-1}$ 2 1.357e+02 Henry's Law Solubility Coefficient 4 1.357 $\pu{atm-1}$ 5 2 2.4815e+02 Ambient temperature 5 2.4815 $\pu{K}$ 1 -2.5e+01 Ambient temperature 2 -2.5 °C -2 2.43e-02 Mole fraction - Liquid (1) 3 2.43 1 2 2.01e+02 Solubility (Pressure per concentration) 3 2.01 $\pu{kPa}$ 0 9.6e+00 Solubility 2 9.6 $\pu{cm3(g) cm-3(s) cmHg-1}$ 1 8.09e+01 Henry's Law Solubility Coefficient 3 8.09 $\pu{atm-1}$ 6 2 2.4815e+02 Ambient temperature 5 2.4815 $\pu{K}$ 1 -2.5e+01 Ambient temperature 2 -2.5 °C -2 4.86e-02 Mole fraction - Liquid (1) 3 4.86 1 2 3.02e+02 Solubility (Pressure per concentration) 3 3.02 $\pu{kPa}$ 1 1.97e+01 Solubility 3 1.97 $\pu{cm3(g) cm-3(s) cmHg-1}$ 1 6.10e+01 Henry's Law Solubility Coefficient 3 6.10 $\pu{atm-1}$ 7 2 2.4815e+02 Ambient temperature 5 2.4815 $\pu{K}$ 1 -2.5e+01 Ambient temperature 2 -2.5 °C -1 1.011e-01 Mole fraction - Liquid (1) 4 1.011 1 2 5.04e+02 Solubility (Pressure per concentration) 3 5.04 $\pu{kPa}$ 1 4.34e+01 Solubility 3 4.34 $\pu{cm3(g) cm-3(s) cmHg-1}$ 1 4.90e+01 Henry's Law Solubility Coefficient 3 4.90 $\pu{atm-1}$ 8 2 2.5815e+02 Ambient temperature 5 2.5815 $\pu{K}$ 1 -1.5e+01 Ambient temperature 2 -1.5 °C -3 6.7e-03 Mole fraction - Liquid (1) 2 6.7 1 2 1.5e+02 Solubility (Pressure per concentration) 2 1.5 $\pu{kPa}$ 0 2.6e+00 Solubility 2 2.6 $\pu{cm3(g) cm-3(s) cmHg-1}$ 2 2.156e+02 Henry's Law Solubility Coefficient 4 2.156 $\pu{atm-1}$ 9 2 2.5815e+02 Ambient temperature 5 2.5815 $\pu{K}$ 1 -1.5e+01 Ambient temperature 2 -1.5 °C -2 1.68e-02 Mole fraction - Liquid (1) 3 1.68 1 2 2.01e+02 Solubility (Pressure per concentration) 3 2.01 $\pu{kPa}$ 0 6.6e+00 Solubility 2 6.6 $\pu{cm3(g) cm-3(s) cmHg-1}$ 2 1.157e+02 Henry's Law Solubility Coefficient 4 1.157 $\pu{atm-1}$ 10 2 2.5815e+02 Ambient temperature 5 2.5815 $\pu{K}$ 1 -1.5e+01 Ambient temperature 2 -1.5 °C -2 3.93e-02 Mole fraction - Liquid (1) 3 3.93 1 2 3.02e+02 Solubility (Pressure per concentration) 3 3.02 $\pu{kPa}$ 1 1.58e+01 Solubility 3 1.58 $\pu{cm3(g) cm-3(s) cmHg-1}$ 1 7.48e+01 Henry's Law Solubility Coefficient 3 7.48 $\pu{atm-1}$ 11 2 2.5815e+02 Ambient temperature 5 2.5815 $\pu{K}$ 1 -1.5e+01 Ambient temperature 2 -1.5 °C -2 8.12e-02 Mole fraction - Liquid (1) 3 8.12 1 2 5.04e+02 Solubility (Pressure per concentration) 3 5.04 $\pu{kPa}$ 1 3.41e+01 Solubility 3 3.41 $\pu{cm3(g) cm-3(s) cmHg-1}$ 1 6.08e+01 Henry's Law Solubility Coefficient 3 6.08 $\pu{atm-1}$ 12 2 2.7815e+02 Ambient temperature 5 2.7815 $\pu{K}$ 0 5e+00 Ambient temperature 1 5 °C -3 2.3e-03 Mole fraction - Liquid (1) 2 2.3 1 2 1.5e+02 Solubility (Pressure per concentration) 2 1.5 $\pu{kPa}$ -1 9e-01 Solubility 1 9 $\pu{cm3(g) cm-3(s) cmHg-1}$ 2 5.85e+02 Henry's Law Solubility Coefficient 3 5.85 $\pu{atm-1}$ 13 2 2.7815e+02 Ambient temperature 5 2.7815 $\pu{K}$ 0 5e+00 Ambient temperature 1 5 °C -3 7.7e-03 Mole fraction - Liquid (1) 2 7.7 1 2 2.01e+02 Solubility (Pressure per concentration) 3 2.01 $\pu{kPa}$ 0 3.0e+00 Solubility 2 3.0 $\pu{cm3(g) cm-3(s) cmHg-1}$ 2 2.42e+02 Henry's Law Solubility Coefficient 3 2.42 $\pu{atm-1}$ 14 2 2.7815e+02 Ambient temperature 5 2.7815 $\pu{K}$ 0 5e+00 Ambient temperature 1 5 °C -2 2.13e-02 Mole fraction - Liquid (1) 3 2.13 1 2 3.02e+02 Solubility (Pressure per concentration) 3 3.02 $\pu{kPa}$ 0 8.4e+00 Solubility 2 8.4 $\pu{cm3(g) cm-3(s) cmHg-1}$ 2 1.34e+02 Henry's Law Solubility Coefficient 3 1.34 $\pu{atm-1}$ 15 2 2.7815e+02 Ambient temperature 5 2.7815 $\pu{K}$ 0 5e+00 Ambient temperature 1 5 °C -2 4.88e-02 Mole fraction - Liquid (1) 3 4.88 1 2 5.04e+02 Solubility (Pressure per concentration) 3 5.04 $\pu{kPa}$ 1 1.98e+01 Solubility 3 1.98 $\pu{cm3(g) cm-3(s) cmHg-1}$ 1 9.96e+01 Henry's Law Solubility Coefficient 3 9.96 $\pu{atm-1}$ 16 2 3.0815e+02 Ambient temperature 5 3.0815 $\pu{K}$ 1 3.5e+01 Ambient temperature 2 3.5 °C -3 3.9e-03 Mole fraction - Liquid (1) 2 3.9 1 2 3.02e+02 Solubility (Pressure per concentration) 3 3.02 $\pu{kPa}$ 0 1.5e+00 Solubility 2 1.5 $\pu{cm3(g) cm-3(s) cmHg-1}$ 2 6.52e+02 Henry's Law Solubility Coefficient 3 6.52 $\pu{atm-1}$ 17 2 3.0815e+02 Ambient temperature 5 3.0815 $\pu{K}$ 1 3.5e+01 Ambient temperature 2 3.5 °C -2 2.25e-02 Mole fraction - Liquid (1) 3 2.25 1 2 5.04e+02 Solubility (Pressure per concentration) 3 5.04 $\pu{kPa}$ 0 8.9e+00 Solubility 2 8.9 $\pu{cm3(g) cm-3(s) cmHg-1}$ 2 2.01e+02 Henry's Law Solubility Coefficient 3 2.01 $\pu{atm-1}$ 18 1 Solubility, Solubility data series The apparatus consisted of an absorber, 10-mL in volume, and a complex system using electrical contacts in a tube for maintaining a constant gas supply pressure in the absorber. The contacts were used to start and stop a gear pump which pumped silicone oil as an 'inert' medium to displace gas from a gas storage vessel. The change in volume of silicone oil utilized was read on a burette and was considered to represent the volume of gas used. The absorber initially contained 3-5 mL of solvent confined in a thin-walled glass ampoule. The chamber was pressurized with gas and to initiate the experiment the ampoule was broken using a stainless steel ball. The International Union of Pure and Applied Chemistry Hronec, M.; Hagara, A.; Ilavsky, J.; Petrochemia, (Czechoslovakia), 1983, 23, 111-115. paper 67-64-1 2 C3H6O InChI=1S/C3H6O/c1-3(2)4/h1-2H3 CSCPPACGZOOCGX-UHFFFAOYSA-N 58.0791 Acetone Acetone was reagent grade with water content small than 0.5%. 74-85-1 1 C2H4 InChI=1S/C2H4/c1-2/h1-2H2 VGGSQFUCUMXWEO-UHFFFAOYSA-N 28.0532 Ethene Ethene purity was 99.8%. Ethene with 2-Propanone