2014
DOI: 10.1016/j.gca.2013.10.018
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A general model for predicting the solubility behavior of H2O–CO2 fluids in silicate melts over a wide range of pressure, temperature and compositions

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Cited by 70 publications
(95 citation statements)
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References 117 publications
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“…Consequently, it may be used in conjunction with these computational packages to model the effects of mixed fluid saturation on liquid-solid phase relations in magmatic systems under crustal pressure (P)-temperature (T) conditions. Internal consistency with MELTS and rhyolite-MELTS discriminates the model presented here from the work of Duan (2014), Papale (1997Papale ( , 1999, Papale et al (2006), , Dixon et al (1995), Newman and Lowenstern (2002), and others (see Table 3 of Moore 2008). Additionally, the described model extends the calibration database of Papale et al (2006) and improves upon the underlying theoretical formulation for activity composition relations of the H 2 O component in the melt (after Ghiorso et al 1983), as well as implementing a more robust and extensible model for the thermodynamic properties of the fluid phase (following Duan and Zhang 2006; this fluid model is also adopted by Duan 2014).…”
mentioning
confidence: 55%
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“…Consequently, it may be used in conjunction with these computational packages to model the effects of mixed fluid saturation on liquid-solid phase relations in magmatic systems under crustal pressure (P)-temperature (T) conditions. Internal consistency with MELTS and rhyolite-MELTS discriminates the model presented here from the work of Duan (2014), Papale (1997Papale ( , 1999, Papale et al (2006), , Dixon et al (1995), Newman and Lowenstern (2002), and others (see Table 3 of Moore 2008). Additionally, the described model extends the calibration database of Papale et al (2006) and improves upon the underlying theoretical formulation for activity composition relations of the H 2 O component in the melt (after Ghiorso et al 1983), as well as implementing a more robust and extensible model for the thermodynamic properties of the fluid phase (following Duan and Zhang 2006; this fluid model is also adopted by Duan 2014).…”
mentioning
confidence: 55%
“…Papale et al (2006) used the thermodynamic model of Kerrick and Jacobs (1981), which is a modified Redlick-Kwong formulation for the H 2 O-CO 2 system. Along with Duan (2014), we choose the model of Duan and Zhang (2006; see ESM Appendix to this paper). This more recent formulation is based on a virial expansion EOS and is therefore more readily extensible to more complex fluids (e.g., plus CH 4 , SO 2 ).…”
Section: The Modelmentioning
confidence: 99%
“…[Note that at a total pressure, P tot , of 1 atm and magmatic temperatures, the behavior of H 2 -CO 2 gas mixtures is so close to ideal that the fugacity of each species in the vapor is essentially equal to its partial pressure (e.g., Jakobsson and Oskarsson 1994;Duan 2014), which is in turn equal to the mole fraction of that species in the vapor (e.g., Deines et al 1974). The assumption of gas ideality will be applied for the remainder of this study, and fugacity and partial pressure will be used interchangeably.]…”
Section: Methodsmentioning
confidence: 99%
“…H 2 is assumed to be insoluble in the melt at the low pressures considered here (see discussion in section 5.3). We assume an oxygen fugacity corresponding to IW−1 at 1350 °C (this fixes the H 2 /H 2 O and CO/CO 2 ratios in the vapor phase; Deines et al 1974), and we assume that the vapor behaves as an ideal mixture of ideal gases, consistent with expectations for the low pressures and high temperatures considered here (Jakobsson and Oskarsson 1994;Duan 2014). The results of these calculations indicate that carbon exsolves from the melt first, followed by water at lower pressures (<~20 bar for the melt containing 4 ppm C and <~50 bar for the melt containing 64 ppm C).…”
Section: Which Volatile Species Likely Dominated In the Vapor That Drmentioning
confidence: 96%
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