2005
DOI: 10.1016/j.gca.2005.01.015
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CO2-H2O mixtures in the geological sequestration of CO2. II. Partitioning in chloride brines at 12–100°C and up to 600 bar

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Cited by 484 publications
(356 citation statements)
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“…The solubility of benzene and CO 2 in water (or brine), on the other hand, is treated with pressure and temperature-dependent equilibrium constants (similar to Henry's coefficients) that rely on experimental data. For CO 2 , aqueous solubilities rely on the solubility model of Spycher and Pruess (2005) (see Appendix A, Section A.1). For benzene, aqueous solubilities are derived using various published data as described in Appendix A, Sections A.2 and A.3.…”
Section: Partitioning Of Benzene Between Co 2 and Watermentioning
confidence: 99%
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“…The solubility of benzene and CO 2 in water (or brine), on the other hand, is treated with pressure and temperature-dependent equilibrium constants (similar to Henry's coefficients) that rely on experimental data. For CO 2 , aqueous solubilities rely on the solubility model of Spycher and Pruess (2005) (see Appendix A, Section A.1). For benzene, aqueous solubilities are derived using various published data as described in Appendix A, Sections A.2 and A.3.…”
Section: Partitioning Of Benzene Between Co 2 and Watermentioning
confidence: 99%
“…The SoaveRedlich-Kwong option of GASEOS was used, with binary interaction parameters for H 2 S and CO 2 from Walas (1985). The solubility of these gases in water are computed using equilibrium constants (i.e., Henry's law at infinite dilution) and activity coefficients using data from Spycher and Pruess (2005) …”
Section: Calculating the Phase Behavior Of The H 2 S + Co 2 + H 2 O Smentioning
confidence: 99%
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“…is the phase change term (i.e., CO 2 dissolution into water and water evaporation into CO 2 ) (Spycher and Pruess, 2005) and  is either CO 2 -rich phase, c , or aqueous phase, w .…”
Section: Thermo-hydro-mechanical Mathematical Modelmentioning
confidence: 99%
“…Equilibrium constants used for aqueous-aqueous and aqueous-mineral reactions in three examples are taken from Wolery (1992). A new fluid property module, ECO2N, based on work of Spycher and Pruess (2005) was used. This module provides an accurate description of the thermophysical properties of mixtures of water and CO 2 under conditions typically encountered in saline aquifers of interest for CO 2 sequestration (31°C  T  110°C; 73.8 bars < P  600 bars).…”
Section: Introductionmentioning
confidence: 99%