Rosa Crovetto 2 2.9315e+02 Ambient temperature 5 2.9315 $\pu{K}$ 1 2.0e+01 Ambient temperature 2 2.0 °C -3 3.208e-03 Mole fraction - Liquid (1) 4 3.208 1 0 5e+00 Ambient pressure 1 5 $\pu{kg/cm2}$ 0 3.97e+00 Bunsen Coefficient 3 3.97 $\pu{cm3(g) cm-3(l) atm-1}$ 1 0 4.903e+00 Pressure (Compiler) 4 4.903 $\pu{bar}$ 2 2.9315e+02 Ambient temperature 5 2.9315 $\pu{K}$ 1 2.0e+01 Ambient temperature 2 2.0 °C -3 6.289e-03 Mole fraction - Liquid (1) 4 6.289 1 1 1e+01 Ambient pressure 1 1 $\pu{kg/cm2}$ 0 7.81e+00 Bunsen Coefficient 3 7.81 $\pu{cm3(g) cm-3(l) atm-1}$ 2 0 9.807e+00 Pressure (Compiler) 4 9.807 $\pu{bar}$ 2 2.9315e+02 Ambient temperature 5 2.9315 $\pu{K}$ 1 2.0e+01 Ambient temperature 2 2.0 °C -3 9.231e-03 Mole fraction - Liquid (1) 4 9.231 1 1 1.5e+01 Ambient pressure 2 1.5 $\pu{kg/cm2}$ 1 1.15e+01 Bunsen Coefficient 3 1.15 $\pu{cm3(g) cm-3(l) atm-1}$ 3 1 1.4710e+01 Pressure (Compiler) 5 1.4710 $\pu{bar}$ 2 2.9315e+02 Ambient temperature 5 2.9315 $\pu{K}$ 1 2.0e+01 Ambient temperature 2 2.0 °C -2 1.1846e-02 Mole fraction - Liquid (1) 5 1.1846 1 1 2e+01 Ambient pressure 1 2 $\pu{kg/cm2}$ 1 1.48e+01 Bunsen Coefficient 3 1.48 $\pu{cm3(g) cm-3(l) atm-1}$ 4 1 1.961e+01 Pressure (Compiler) 4 1.961 $\pu{bar}$ 2 2.9315e+02 Ambient temperature 5 2.9315 $\pu{K}$ 1 2.0e+01 Ambient temperature 2 2.0 °C -2 1.641e-02 Mole fraction - Liquid (1) 4 1.641 1 1 3e+01 Ambient pressure 1 3 $\pu{kg/cm2}$ 1 2.06e+01 Bunsen Coefficient 3 2.06 $\pu{cm3(g) cm-3(l) atm-1}$ 5 1 2.942e+01 Pressure (Compiler) 4 2.942 $\pu{bar}$ 2 3.0315e+02 Ambient temperature 5 3.0315 $\pu{K}$ 1 3.0e+01 Ambient temperature 2 3.0 °C -3 2.772e-03 Mole fraction - Liquid (1) 4 2.772 1 0 5e+00 Ambient pressure 1 5 $\pu{kg/cm2}$ 0 3.42e+00 Bunsen Coefficient 3 3.42 $\pu{cm3(g) cm-3(l) atm-1}$ 6 0 4.903e+00 Pressure (Compiler) 4 4.903 $\pu{bar}$ 2 3.0315e+02 Ambient temperature 5 3.0315 $\pu{K}$ 1 3.0e+01 Ambient temperature 2 3.0 °C -3 7.786e-03 Mole fraction - Liquid (1) 4 7.786 1 1 1.5e+01 Ambient pressure 2 1.5 $\pu{kg/cm2}$ 0 9.66e+00 Bunsen Coefficient 3 9.66 $\pu{cm3(g) cm-3(l) atm-1}$ 7 1 1.4710e+01 Pressure (Compiler) 5 1.4710 $\pu{bar}$ 2 3.0315e+02 Ambient temperature 5 3.0315 $\pu{K}$ 1 3.0e+01 Ambient temperature 2 3.0 °C -3 9.970e-03 Mole fraction - Liquid (1) 4 9.970 1 1 2e+01 Ambient pressure 1 2 $\pu{kg/cm2}$ 1 1.24e+01 Bunsen Coefficient 3 1.24 $\pu{cm3(g) cm-3(l) atm-1}$ 8 1 1.961e+01 Pressure (Compiler) 4 1.961 $\pu{bar}$ 2 3.0315e+02 Ambient temperature 5 3.0315 $\pu{K}$ 1 3.0e+01 Ambient temperature 2 3.0 °C -2 1.495e-02 Mole fraction - Liquid (1) 4 1.495 1 1 3e+01 Ambient pressure 1 3 $\pu{kg/cm2}$ 1 1.87e+01 Bunsen Coefficient 3 1.87 $\pu{cm3(g) cm-3(l) atm-1}$ 9 1 2.942e+01 Pressure (Compiler) 4 2.942 $\pu{bar}$ 1 Solubility, Solubility data series A 'conventional' high pressure apparatus was used. Equilibrium in the system was attained by bubbling gas at constant pressure. The equilibrium composition in the system was determined by measuring the volume of water, and the pressure and volume of the dissolved $\ce{CO2}$ in a buret that was thermostatted. The solubilities of the gas mixtures $\ce{CO2}-\ce{H2}$ were also measured with the same experimental apparatus. Details are given in the source. The authors calculated the fugacity of the pure gas from [1]. The International Union of Pure and Applied Chemistry Jellinek, K.; Lehrbuch der Physikalischen Chemie, Bd. 4, 1933, 231. paper Kritschewsky, I. R.; Shaworonkoff, N. M.; Aepelbaum, V. A.; Z. Phys. Chem. 1935, 175, 232-8. paper https://doi.org/10.1515/zpch-1935-17518 124-38-9 1 CO2 InChI=1S/CO2/c2-1-3 CURLTUGMZLYLDI-UHFFFAOYSA-N 44.0095 Carbon dioxide Nothing specified. 7732-18-5 2 H2O InChI=1S/H2O/h1H2 XLYOFNOQVPJJNP-UHFFFAOYSA-N 18.0153 Water Carbon dioxide with Water