2007
DOI: 10.1016/j.gca.2006.08.038
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Quartz solubility in the two-phase and critical region of the NaCl–KCl–H2O system: Implications for submarine hydrothermal vent systems at 9°50′N East Pacific Rise

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Cited by 60 publications
(80 citation statements)
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“…The measured and of the Kulo Lasi fluids are almost on the critical curve of seawater meaning that liquid and vapor phase may coexist at Kulo Lasi. An adiabatic decompression of supercritical seawater (initial fluid and equivalent to 3.2 wt% NaCl) as it rises towards the seafloor would cause it to separate, at about 320-350 bar and 415-420 ∘ C, into two phases having the NaCl percentages observed at Kulo Lasi ( Figure S3) [53,54].…”
Section: Chlorinitymentioning
confidence: 99%
“…The measured and of the Kulo Lasi fluids are almost on the critical curve of seawater meaning that liquid and vapor phase may coexist at Kulo Lasi. An adiabatic decompression of supercritical seawater (initial fluid and equivalent to 3.2 wt% NaCl) as it rises towards the seafloor would cause it to separate, at about 320-350 bar and 415-420 ∘ C, into two phases having the NaCl percentages observed at Kulo Lasi ( Figure S3) [53,54].…”
Section: Chlorinitymentioning
confidence: 99%
“…The solubility of quartz in hydrothermal solutions is a strong function of temperature, pressure and to a lesser extent, salinity. Based on the assumption of quartz-fluid equilibrium at depth, dissolved SiO 2 is commonly used as an indicator of maximum P-T conditions encountered by hydrothermal fluids (Fournier, 1983;Von Damm et al, 1991;Foustoukos and Seyfried, 2007a). Using extrapolated (to zero Mg) vent temperatures and the quartz solubility data of (Von Damm et al, 1991), and SiO 2 contents, RMR2 and RGR1 compositions suggest quartz-fluid equilibrium at pressure of 400-700 bar (Fig.…”
Section: Quartz-fluid Equilibrium and Dissolved Siomentioning
confidence: 99%
“…The high precision pressure transducer is accompanied with a NIST traceable certificate of calibration (www.heise.com), limiting pressure uncertainties to 0.025% of the operating pressure. Temperature uncertainties are ±1°C based on previous calibrations conducted with steam-saturated water at 300-360°C (Foustoukos and Seyfried, 2007). Both temperature and pressure measurements were digitally recorded through RS-232 communications, allowing P-T conditions to be continuously monitored during the length of fluid flow and sampling procedure.…”
Section: Experimental Procedures and Designmentioning
confidence: 99%
“…Thermodynamic data for the Rb, Cs and Br aqueous species (Rb + , Cs + , Br À , RbCl (aq) , RbBr (aq) , RbOH (aq) , CsCl (aq) , CsOH (aq) , CsBr (aq) , NaBr (aq) ) were retrieved from Sverjensky et al (1997) and Shock et al (1997), whereas for the B aqueous species (BðOHÞ 4 À , B(OH) 3(aq) , NaB(OH) 4(aq) ) data were derived from Pokrovski et al (1995). Activity coefficients for charged aqueous species were calculated using the extended Davies model (Davies, 1962) following methodologies described in Foustoukos and Seyfried (2007).…”
Section: Theoretical Modelingmentioning
confidence: 99%
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