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Basic Research Needs for Geosciences - Energetics Meetings and ...

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GRAND CHALLENGE: COMPUTATIONAL THERMODYNAMICS OF COMPLEX FLUIDS AND SOLIDSCourtesy of John Weare, UC San DiegoFigure 26. Pressure-composition predictions of EOS <strong>for</strong> the CO 2 -H 2 O system. Curves represent EOS predictions<strong>and</strong> symbols represent experimental data.EOS <strong>for</strong> compressible mixtures. For these systems the most convenient variables are usually thetemperature, volume (or density), <strong>and</strong> the composition. The appropriate thermodynamic functionon which to base an EOS is then the molar Helmholtz free energy. All other properties, e.g., theenthalpy, may be derived from this function by the appropriate derivatives. To provide optimalinterpolation <strong>and</strong> extrapolation of mixing properties, the functional <strong>for</strong>m of the free energyshould be based on a reasonably accurate molecular-level description of the system. Thethermodynamic perturbation theory originally introduced by Pople (1954) provides a frameworkfrom which such an EOS may be generated (see Gubbins 1985 <strong>for</strong> a review). To provide the highlevel of accuracy necessary <strong>for</strong> quantitative description of thermodynamic data, empiricalcorrections must usually be added to the EOS. This level of the theory was successfully appliedto the qualitative analysis of polar fluids <strong>and</strong> has been used to treat polar systems including thosecontaining associated ions. An example of the accuracy that can be obtained from such anapproach is given in Figure 26 (Weare, unpublished results based on the EOS of Duan et al.1992). Note the poor behavior of the EOS in the critical region. Special scaling methods must bedeveloped to treat this region (Kiselev <strong>and</strong> Friend 1999). The development of these methods willbe required <strong>for</strong> application to complex speciation in mixtures.EOS <strong>for</strong> liquid density complex mixtures of aqueous electrolyte solutions <strong>and</strong> mixtures with othernonaqueous solutions. For nearly incompressible aqueous mixtures, highly accurate EOS areavailable provided the mixing behavior of the system can be described (Pitzer 1987; Weare1987; Christov <strong>and</strong> Moller 2004). Examples of the results of these models <strong>for</strong> complex mixturesare illustrated in Figure 27.<strong>Basic</strong> <strong>Research</strong> <strong>Needs</strong> <strong>for</strong> <strong>Geosciences</strong>: Facilitating 21 st Century Energy Systems 75

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