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4.3  Application Examples of the Term Splitting Algorithm       83

            Fig. 4.1 Geometry and                     3000 m
            initial conditions for the
            fluid-rock interaction
            problem in a pore-fluid
            saturated aquifer      CO          99% Quartz + 1% K-feldspar  1000 m
                                     2
                                               φ 0 =  , 1 . 0  u x0 = 10  8 −  m/ s



            ple considered in this section is an isothermal fluid-rock interaction problem in a
            pore-fluid saturated horizontal aquifer within a sedimentary basin. The topographi-
            cally induced pore-fluid flow is horizontally from the left to the right of the aquifer.
            This means that the horizontal Darcy velocity is constant within the aquifer. The
            rock of the aquifer is initially composed of K-feldspar (KAlSi 3 O 8 ) and quartz (SiO 2 ).
            There is an injection of carbon dioxide gas (CO 2 ) at the left inlet of the aquifer. The
            injected carbon dioxide flow in the aquifer may dissolve K-feldspar and precipitate
            muscovite (KAl 3 Si 3 O 10 (OH) 2 ). If the injected carbon dioxide flow is strong enough,
            the precipitated muscovite may be dissolved and pyrophyllite (Al 2 Si 4 O 10 (OH) 2 )
            will be precipitated. Basically, the following three overall chemical reactions may
            take place in the aquifer.

                                           fast
                                                        +
                                                  −
                                CO 2 + H 2 O =⇒ HCO + H ,                (4.22)
                                                  3
                                   k 1
                                        +
                                +
                  3KAlSi 3 O 8 + 2H =⇒ 2K + KAl 3 Si 3 O 10 (OH) 2 + 6SiO 2 ,  (4.23)
                                              k 2
                                                   +
               2KAl 3 Si 3 O 10 (OH) 2 + 2H + 6SiO 2 =⇒ 2K + 3Al 2 Si 4 O 10 (OH) 2 .  (4.24)
                                    +
              The first reaction (i.e. Eq. (4.22)) states that when the injected carbon dioxide
            (CO 2 ) gas enters the fluid-rock system, it reacts very fast with water (H 2 O), so that
            the chemical equilibrium can be reached quasi-instantaneously. This means that the
            injection of carbon dioxide (CO 2 ) gas is equivalent to the direct injection of H into
                                                                         +
            the system. As will be demonstrated later, the use of this equivalence may result in
            a reduction in the number of primary reactive chemical species and therefore, a
            considerable reduction in the degrees of freedom of the whole system. As a direct
            consequence, the number of reactive species transport equations can be reduced to
            the minimum in computation. This can lead to a significant reduction in require-
            ments of both the computer storage and CPU time in the numerical modelling of
            fluid-rock interaction problems.
              It needs to be pointed out that Eq. (4.23) describes a heterogeneous chem-
            ical reaction, in which K-feldspar (KAlSi 3 O 8 ) is dissolved and muscovite
            (KAl 3 Si 3 O 10 (OH) 2 ) is precipitated, while Eq. (4.24) describes a heterogeneous
            chemical reaction, in which muscovite (KAl 3 Si 3 O 10 (OH) 2 ) is dissolved and pyro-
            phyllite (Al 2 Si 4 O 10 (OH) 2 ) is precipitated in the fluid-rock system. Chemically,
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