Page 53 - Fundamentals of Computational Geoscience Numerical Methods and Algorithms
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3.1  Statement of the Coupled Problem and Solution Method       39

            problem describing the steady-state pore-fluid flow, heat transfer and mass trans-
            port/chemical reactions in a porous medium, the corresponding governing equations
            are expressed as follows:

                                       ∂u   ∂v
                                          +    = 0,                       (3.1)
                                       ∂x   ∂y


                                         K x   ∂P
                                     u =      −     ,                     (3.2)
                                          μ    ∂x

                                      K y   ∂P
                                  v =      −   + ρ f g ,                  (3.3)
                                       μ     ∂y
                                                   2        2
                                  ∂T    ∂T        ∂ T      ∂ T
                          ρ f 0 c  u  + v                     ,           (3.4)
                              p              = λ ex  2  + λ ey  2
                                  ∂x     ∂y       ∂x       ∂y

                                         2         2
                  ∂C i   ∂C i           ∂ C i     ∂ C i
            ρ f 0 u   + v     = ρ f 0 D ex   + D ey     + φR i  (i = 1, 2, ..., N),
                  ∂x     ∂y              ∂x 2      ∂y 2
                                                                          (3.5)
                                                  N


                         ρ f = ρ f 0 1 − β T (T − T 0 ) −  β Ci (C i − C 0 ) ,  (3.6)
                                                 i=1
                      λ ex = φλ fx + (1 − φ)λ sx ,  λ ey = φλ fy + (1 − φ)λ sy ,  (3.7)

                                D ex = φD fx ,  D ey = φD fy ,            (3.8)

            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 temper-
            ature of the porous medium; C i is the normalized concentration (in a mass fraction
            form relative to the pore-fluid density) of chemical species i; N is the total num-
            ber 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 is the density of the pore-fluid and g is
            the acceleration due to gravity; ρ f 0 , T 0 and C 0 are the reference density, reference
            temperature and reference normalized concentration of the chemical species 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 p is the specific heat of the pore-fluid; D fx and
            D fx are the diffusivities of the chemical species in the x and y directions respec-
            tively; φ is the porosity of the porous medium; β T and β Ci are the thermal volume
            expansion coefficient of the pore-fluid and the volumetric expansion coefficient due
            to chemical species i; R i is the chemical reaction term for the transport equation of
            chemical species i.
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