Andrzej Maczynski 2 3.59e+02 Ambient temperature 3 3.59 $\pu{K}$ 1 2.5e+01 Ambient pressure 2 2.5 psia -1 1.7e-01 Ambient pressure 2 1.7 $\pu{MPa}$ -1 3.3e-01 Relative mass - solution (2) 2 3.3 g₁/100 g₂ 1 -2 1.4e-02 Mole fraction - Liquid (2) 2 1.4 1 2 3.85e+02 Ambient temperature 3 3.85 $\pu{K}$ 1 5.0e+01 Ambient pressure 2 5.0 psia -1 3.4e-01 Ambient pressure 2 3.4 $\pu{MPa}$ -1 6.3e-01 Relative mass - solution (2) 2 6.3 g₁/100 g₂ 2 -2 2.7e-02 Mole fraction - Liquid (2) 2 2.7 1 2 4.13e+02 Ambient temperature 3 4.13 $\pu{K}$ 2 1.00e+02 Ambient pressure 3 1.00 psia -1 6.9e-01 Ambient pressure 2 6.9 $\pu{MPa}$ 0 1.08e+00 Relative mass - solution (2) 3 1.08 g₁/100 g₂ 3 -2 4.5e-02 Mole fraction - Liquid (2) 2 4.5 1 2 4.34e+02 Ambient temperature 3 4.34 $\pu{K}$ 2 1.50e+02 Ambient pressure 3 1.50 psia 0 1.03e+00 Ambient pressure 3 1.03 $\pu{MPa}$ 0 1.54e+00 Relative mass - solution (2) 3 1.54 g₁/100 g₂ 4 -2 6.4e-02 Mole fraction - Liquid (2) 2 6.4 1 2 4.43e+02 Ambient temperature 3 4.43 $\pu{K}$ 2 2.00e+02 Ambient pressure 3 2.00 psia 0 1.38e+00 Ambient pressure 3 1.38 $\pu{MPa}$ 0 1.75e+00 Relative mass - solution (2) 3 1.75 g₁/100 g₂ 5 -2 7.2e-02 Mole fraction - Liquid (2) 2 7.2 1 2 4.53e+02 Ambient temperature 3 4.53 $\pu{K}$ 2 2.50e+02 Ambient pressure 3 2.50 psia 0 1.72e+00 Ambient pressure 3 1.72 $\pu{MPa}$ 0 2.08e+00 Relative mass - solution (2) 3 2.08 g₁/100 g₂ 6 -2 8.4e-02 Mole fraction - Liquid (2) 2 8.4 1 2 4.61e+02 Ambient temperature 3 4.61 $\pu{K}$ 2 3.00e+02 Ambient pressure 3 3.00 psia 0 2.07e+00 Ambient pressure 3 2.07 $\pu{MPa}$ 0 2.25e+00 Relative mass - solution (2) 3 2.25 g₁/100 g₂ 7 -2 9.1e-02 Mole fraction - Liquid (2) 2 9.1 1 2 4.69e+02 Ambient temperature 3 4.69 $\pu{K}$ 2 3.50e+02 Ambient pressure 3 3.50 psia 0 2.41e+00 Ambient pressure 3 2.41 $\pu{MPa}$ 0 2.60e+00 Relative mass - solution (2) 3 2.60 g₁/100 g₂ 8 -1 1.04e-01 Mole fraction - Liquid (2) 3 1.04 1 2 4.73e+02 Ambient temperature 3 4.73 $\pu{K}$ 2 4.00e+02 Ambient pressure 3 4.00 psia 0 2.76e+00 Ambient pressure 3 2.76 $\pu{MPa}$ 0 2.80e+00 Relative mass - solution (2) 3 2.80 g₁/100 g₂ 9 -1 1.11e-01 Mole fraction - Liquid (2) 3 1.11 1 1 Solubility, Solubility data series The measurements were carried out in the autoclave for vapor-liquid equilibrium determination. The solubility points were obtained by incremental addition of (2) followed by stirring, settling, sampling and analysis. This procedure was continued until addition of water resulted in no pressure increase, indicating three-phase conditions. The samples were analyzed by glc. The International Union of Pure and Applied Chemistry Burd Jr., S. D.; Braun, W. G.; Proc. Div. Refining.; Am. Petrol. Inst. 1968, 48, 464-76. paper 7732-18-5 2 H2O InChI=1S/H2O/h1H2 XLYOFNOQVPJJNP-UHFFFAOYSA-N 18.0153 Water distilled 71-43-2 1 C6H6 InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H UHOVQNZJYSORNB-UHFFFAOYSA-N 78.1118 Benzene Phillips Petroleum Co.; 99.0% by GLC; used as received. Benzene with Water