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American Mineralogist; October 2004; v. 89; no. 10; p. 1447-1455
© 2004 Mineralogical Society of America
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The CO2–H2O system: IV. Empirical, isothermal equations for representing vapor-liquid equilibria at 110–350 °C, P ≤ 150 MPa

James G. Blencoe*

Chemical Sciences Division, Oak Ridge National Laboratory, P.O. Box 2008, Building 4500-S, Oak Ridge, Tennessee 37831-6110, U.S.A.

Correspondence: * E-mail: blencoejg{at}ornl.gov

Empirical formulae are presented for calculating vapor-liquid equilibria (VLE) in the CO2-H2O system at 10 temperatures between 110 and 350 °C. At each temperature, separate functions are used to represent the bubble- and dew-point boundary curves that: originate at the saturation vapor pressure of water (PsatH2O) at XCO2 = 0; diverge with increasing pressure up to ~P (XCO2max) where {partial}P/{partial}XCO2 = +{infty} along the dew-point curve; then converge with increasing pressure above P(XCO2max). At temperatures below 265 °C and pressures > P(XCO2max), the compositions of coexisting liquid and vapor [ XCO2L(V) and XCO2V(L)] do not converge completely with increasing pressure due to the absence of critical behavior. Thus, relatively simple functions suffice to accurately represent VLE at those temperatures. In contrast, at T > 265 °C, XCO2L(V) and XCO2V(L) converge rapidly as P approaches Pc (the critical pressure in the CO2-H2O system at a given temperature between 265 and 374 °C and P ≤ 215 MPa). For those temperatures, therefore, more complex VLE formulae are required to achieve close representation of phase relations. For dew-point equations, this includes adding an exponential "correction term" to ensure that {partial}P/{partial}XCO2 = 0 at the critical points indicated by corresponding bubble-point functions.

Stable liquid-vapor coexistence in mixed-volatile systems requires fLi = fVI (isofugacity conditions) for all "i" (volatile components) in the two fluid phases. Thus, the equations presented in this paper specify numerous P-T-X conditions where fH2OL = fH2OV and fCO2L = fCO2V in the CO2-H2O system. These results have important applications in the ongoing effort to develop a more rigorous thermodynamic model for CO2-H2O fluids at geologically relevant temperatures and pressures.







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