Evaluating the feasibility of CO
2 geologic sequestration requires the use of pressure-temperature-composition (
P-
T-
X) data for mixtures of CO
2 and H
2O at moderate pressures and temperatures (typically below 500 bar and below 100°C). For this purpose, published experimental
P-
T-
X data in this temperature and pressure range are reviewed. These data cover the two-phase region where a CO
2-rich phase (generally gas) and an H
2O-rich liquid coexist and are reported as the mutual solubilities of H
2O and CO
2 in the two coexisting phases. For the most part, mutual solubilities reported from various sources are in good agreement. In this paper, a noniterative procedure is presented to calculate the composition of the compressed CO
2 and liquid H
2O phases at equilibrium, based on equating chemical potentials and using the Redlich-Kwong equation of state to express departure from ideal behavior. The procedure is an extension of that used by King et al. (1992), covering a broader range of temperatures and experimental data than those authors, and is readily expandable to a nonideal liquid phase. The calculation method and formulation are kept as simple as possible to avoid degrading the performance of numerical models of water-CO
2 flows for which they are intended. The method is implemented in a computer routine, and inverse modeling is used to determine, simultaneously, (1) new Redlich-Kwong parameters for the CO
2-H
2O mixture, and (2) aqueous solubility constants for gaseous and liquid CO
2 as a function of temperature. In doing so, mutual solubilities of H
2O from 15 to 100°C and CO
2 from 12 to 110°C and up to 600 bar are generally reproduced within a few percent of experimental values. Fugacity coefficients of pure CO
2 are reproduced mostly within one percent of published reference data.
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