Walter Hayduk 2 2.7315e+02 Ambient temperature 5 2.7315 $\pu{K}$ -1 6.3e-01 Percent mass fraction (1) 2 6.3 1 -2 2.04e-02 Mole fraction - Liquid (1) 3 2.04 1 -1 1.013e-01 Ambient pressure 4 1.013 $\pu{MPa}$ -1 5.5e-01 Henry's Law Solubility Coefficient 2 5.5 1 1 2 2.7315e+02 Ambient temperature 5 2.7315 $\pu{K}$ 0 1.3e+00 Percent mass fraction (1) 2 1.3 1 -2 4.15e-02 Mole fraction - Liquid (1) 3 4.15 1 -1 2.026e-01 Ambient pressure 4 2.026 $\pu{MPa}$ -1 5.5e-01 Henry's Law Solubility Coefficient 2 5.5 1 2 2 2.7315e+02 Ambient temperature 5 2.7315 $\pu{K}$ 0 1.9e+00 Percent mass fraction (1) 2 1.9 1 -2 5.98e-02 Mole fraction - Liquid (1) 3 5.98 1 -1 3.040e-01 Ambient pressure 4 3.040 $\pu{MPa}$ -1 5.5e-01 Henry's Law Solubility Coefficient 2 5.5 1 3 2 2.7315e+02 Ambient temperature 5 2.7315 $\pu{K}$ 0 2.7e+00 Percent mass fraction (1) 2 2.7 1 -2 8.35e-02 Mole fraction - Liquid (1) 3 8.35 1 -1 4.053e-01 Ambient pressure 4 4.053 $\pu{MPa}$ -1 5.5e-01 Henry's Law Solubility Coefficient 2 5.5 1 4 2 2.9315e+02 Ambient temperature 5 2.9315 $\pu{K}$ -1 4.5e-01 Percent mass fraction (1) 2 4.5 1 -2 1.46e-02 Mole fraction - Liquid (1) 3 1.46 1 -1 1.013e-01 Ambient pressure 4 1.013 $\pu{MPa}$ -1 4.0e-01 Henry's Law Solubility Coefficient 2 4.0 1 5 2 2.9315e+02 Ambient temperature 5 2.9315 $\pu{K}$ -1 9.0e-01 Percent mass fraction (1) 2 9.0 1 -2 2.90e-02 Mole fraction - Liquid (1) 3 2.90 1 -1 2.026e-01 Ambient pressure 4 2.026 $\pu{MPa}$ -1 4.0e-01 Henry's Law Solubility Coefficient 2 4.0 1 6 2 2.9315e+02 Ambient temperature 5 2.9315 $\pu{K}$ 0 1.4e+00 Percent mass fraction (1) 2 1.4 1 -2 4.46e-02 Mole fraction - Liquid (1) 3 4.46 1 -1 3.040e-01 Ambient pressure 4 3.040 $\pu{MPa}$ -1 4.0e-01 Henry's Law Solubility Coefficient 2 4.0 1 7 2 2.9315e+02 Ambient temperature 5 2.9315 $\pu{K}$ 0 1.9e+00 Percent mass fraction (1) 2 1.9 1 -2 5.98e-02 Mole fraction - Liquid (1) 3 5.98 1 -1 4.053e-01 Ambient pressure 4 4.053 $\pu{MPa}$ -1 4.0e-01 Henry's Law Solubility Coefficient 2 4.0 1 8 2 3.0815e+02 Ambient temperature 5 3.0815 $\pu{K}$ -1 3.5e-01 Percent mass fraction (1) 2 3.5 1 -2 1.14e-02 Mole fraction - Liquid (1) 3 1.14 1 -1 1.013e-01 Ambient pressure 4 1.013 $\pu{MPa}$ -1 3.0e-01 Henry's Law Solubility Coefficient 2 3.0 1 9 2 3.0815e+02 Ambient temperature 5 3.0815 $\pu{K}$ -1 7.0e-01 Percent mass fraction (1) 2 7.0 1 -2 2.26e-02 Mole fraction - Liquid (1) 3 2.26 1 -1 2.026e-01 Ambient pressure 4 2.026 $\pu{MPa}$ -1 3.0e-01 Henry's Law Solubility Coefficient 2 3.0 1 10 2 3.0815e+02 Ambient temperature 5 3.0815 $\pu{K}$ 0 1.1e+00 Percent mass fraction (1) 2 1.1 1 -2 3.52e-02 Mole fraction - Liquid (1) 3 3.52 1 -1 3.040e-01 Ambient pressure 4 3.040 $\pu{MPa}$ -1 3.0e-01 Henry's Law Solubility Coefficient 2 3.0 1 11 2 3.0815e+02 Ambient temperature 5 3.0815 $\pu{K}$ 0 1.5e+00 Percent mass fraction (1) 2 1.5 1 -2 4.76e-02 Mole fraction - Liquid (1) 3 4.76 1 -1 4.053e-01 Ambient pressure 4 4.053 $\pu{MPa}$ -1 3.0e-01 Henry's Law Solubility Coefficient 2 3.0 1 12 2 3.2315e+02 Ambient temperature 5 3.2315 $\pu{K}$ -1 2.5e-01 Percent mass fraction (1) 2 2.5 1 -3 8.16e-03 Mole fraction - Liquid (1) 3 8.16 1 -1 1.013e-01 Ambient pressure 4 1.013 $\pu{MPa}$ -1 2.0e-01 Henry's Law Solubility Coefficient 2 2.0 1 13 2 3.2315e+02 Ambient temperature 5 3.2315 $\pu{K}$ -1 5.0e-01 Percent mass fraction (1) 2 5.0 1 -2 1.62e-02 Mole fraction - Liquid (1) 3 1.62 1 -1 2.026e-01 Ambient pressure 4 2.026 $\pu{MPa}$ -1 2.0e-01 Henry's Law Solubility Coefficient 2 2.0 1 14 2 3.2315e+02 Ambient temperature 5 3.2315 $\pu{K}$ -1 7.5e-01 Percent mass fraction (1) 2 7.5 1 -2 2.42e-02 Mole fraction - Liquid (1) 3 2.42 1 -1 3.040e-01 Ambient pressure 4 3.040 $\pu{MPa}$ -1 2.0e-01 Henry's Law Solubility Coefficient 2 2.0 1 15 2 3.2315e+02 Ambient temperature 5 3.2315 $\pu{K}$ 0 1.1e+00 Percent mass fraction (1) 2 1.1 1 -2 3.52e-02 Mole fraction - Liquid (1) 3 3.52 1 -1 4.053e-01 Ambient pressure 4 4.053 $\pu{MPa}$ -1 2.0e-01 Henry's Law Solubility Coefficient 2 2.0 1 16 1 Solubility, Solubility data series The source of the data was stated to be [1]. Only a graph is available in that reference. It was also stated that the Hoechst company (Germany) used these values of solubility.<br/>There were no details of apparatus or procedure. The International Union of Pure and Applied Chemistry Bier, G.; Lehmann, G.; 'Copolymerization' Chap. IVB of High Polymers, G. Ham, Ed. 1964, Vol. XVIII Interscience, New York, 169 book Frank, V. H. P.; Österr. Chemik. - Zeitung 1967, 68, 360-361. paper 74-85-1 1 C2H4 InChI=1S/C2H4/c1-2/h1-2H2 VGGSQFUCUMXWEO-UHFFFAOYSA-N 28.0532 Ethene Sources and purities not specified. 108-88-3 2 C7H8 InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3 YXFVVABEGXRONW-UHFFFAOYSA-N 92.1384 Toluene Ethene with Methylbenzene