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À propos de : Phase Equilibria, Excess Properties, and Henry's Constants of the Water + Carbon DioxideBinary Mixture        

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  • Phase Equilibria, Excess Properties, and Henry's Constants of the Water + Carbon DioxideBinary Mixture
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  • The high-pressure phase diagram and other thermodynamic properties of the water + carbon dioxide binarymixture are examined using the SAFT-VR approach. The carbon dioxide molecule is modeled as two sphericalsegments tangentially bonded. The water molecule is modeled as a spherical segment with four associatingsites to represent the hydrogen bonding. Dispersive interactions are modeled using the square-wellintermolecular potential. The polar and quadrupolar interactions present in water and carbon dioxide aretreated in an effective way via square-well potentials of variable range. The optimized intermolecular parametersare taken from the works of Galindo and Blas (Fluid Phase Equilib.2002, 194−197, 502; J. Phys. Chem. B2002, 106, 4503) and Clark et al. (Mol. Phys.2006, 22−24, 3561) for carbon dioxide and water, respectively.The phase diagram of the mixture exhibits a number of interesting features: type-III phase behavior accordingto the classification of Scott and Konynenburg, three-phase behavior at low temperatures with its correspondingupper critical end point, a gas−liquid critical line at high temperatures and pressures that continuously changesfrom gas−liquid to liquid−liquid as the pressure is increased and gas−gas immiscibility of second kind.Only one unlike interaction parameter is fitted to give the best possible representation of the temperatureminimum of the gas−liquid critical line of the mixture. This unlike parameter is then used in a transferablemanner to study the complete pressure−temperature−composition phase diagram. The phase diagram calculatedwith SAFT-VR is in excellent agreement with the experimental data taken from the literature in a wide rangeof thermodynamic conditions. The theory is also able to predict a good qualitative description of the excessmolar volume and enthalpy of the mixture as well as the most important features of the Henry's constants atdifferent temperatures.
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