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124        6 Fluid Mixing, Heat Transfer and Non-Equilibrium Redox Chemical Reactions

                     λ ex = φλ fx + (1 − φ)λ sx ,  λ ey = φλ fy + (1 − φ)λ sy ,  (6.7)


                               D ex = φD fx ,   D ey = φD fy ,            (6.8)

            where u and v are the horizontal and vertical velocity components of the pore-fluid in
            the x and y directions respectively; P is the pore-fluid pressure; T is the temperature
            of the porous medium; C i is the concentration of chemical species i; N is the total
            number of the active chemical species considered in the pore-fluid; K x and K y are
            the permeabilities of the porous medium in the x and y directions respectively; μ is
            the dynamic viscosity of the pore-fluid; ρ f and ρ s are the densities of the pore-fluid
            and solid matrix; g is the acceleration due to gravity; ρ f 0 and T 0 are the reference
            density and reference temperature used in the analysis; λ fx and λ sx are the thermal
            conductivities of the pore-fluid and solid matrix in the x direction; λ fy and λ sy are the
            thermal conductivities of the pore-fluid and solid matrix in the y direction; c pf and
            c ps are the specific heat of the pore-fluid and solid matrix respectively; D fx and D fx
            are the diffusivities of the chemical species in the x and y directions respectively; φ is
            the porosity of the porous medium; β T is the thermal volume expansion coefficient
            of the pore-fluid; R i is the source/sink term for the reactive transport equation of
            chemical species i.
              It is noted that if the aqueous mineral concentrations associated with ore body
            formation and mineralization are relatively small, their contributions to the density
            of the pore-fluid are negligible so that the mass transport process can be decoupled
            from the pore-fluid flow and heat transfer processes. This means that the whole cou-
            pled problem between fluids mixing, heat transfer and redox chemical reactions in
            fluid-saturated porous rocks can be divided into two new problems. The first is a
            coupled problem between the pore-fluid flow and the heat transfer process, while
            the second is a coupled problem between the mass transport process and the redox
            chemical reaction process. Since the first coupled problem, which is described by
            Eqs. (6.1), (6.2), (6.3) and (6.4), can be solved using the existing finite element
            method (Lewis and Schrefler 1998, Zienkiewicz 1977), the main purpose of this
            study is to develop a new decoupling procedure to effectively and efficiently solve
            the second coupled problem, which is described by Eq. (6.5) and the related chemi-
            cal reaction equations.
              If the reaction term in Eq. (6.5) can be determined and is linearly dependent
            on the chemical species concentration, then the coupled problem defined between
            fluids mixing, heat transfer and redox chemical reactions in fluid-saturated porous
            rocks above is solvable using the numerical methods available (Zhao et al. 1998a,
            2003a). This requires that the chemical reaction be of the first order. Since many
            chemical reactions of different orders are associated with ore body formation and
            mineralization in fluid-saturated porous rocks, both the second order and the high
            order chemical reactions are very common in nature. Without loss of generality, the
            second order redox chemical reaction is considered in order to develop a concept
            resulting in a new decoupling procedure for removing the coupling between reac-
            tive transport equations of redox chemical reactions. In principle, the new concept
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