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Heat and mass transfers in the context of energy geostructures  113


                   flow gradients for higher temperatures. This is another feature characterising the cou-
                   pling between the thermal and hydraulic behaviours of materials.


                   3.12 Mass conservation equation
                   3.12.1 General

                   The mass conservation equation expresses the principle of conservation of mass. Such
                   an expression, in particular, establishes a relation between the kinematic characteristics
                   of a fluid’s motion and the density of the fluid. This conservation equation is also
                   termed the continuity equation.

                   3.12.2 Mass conservation equation

                   The mass conservation equation can be derived for a representative volume in which
                   mass flows in and out, subjected to arbitrary hydraulic conditions on its surfaces with
                   internal volumetric mass generation _q per unit time (cf. Fig. 3.19). The balance for
                                                    v
                   the elementary volume, as performed for the energy conservation equation, reads

                      Rate of mass entering through  1    Rate of mass    5     Rate of mass
                    the bounding surfaces of a volume  generation in a volume  storage in a volume


                      Accordingly, the mass conservation equation reads
                                                                 @ρ

                                             2 r  ρ v rf ;i 1 _q 5  f                    ð3:41Þ
                                                     f        v
                                                                  @t
                      In many practical cases, no volumetric mass generation is considered. Often the
                   fluid is also assumed incompressible. The hypothesis of incompressibility indicates that
                   the density of the fluid remains constant in space and over time. Based on the above,
                   Eq. (3.41) can be rewritten as

                                                    r  v rf ;i 5 0                       ð3:42Þ




                                                          dx
                                                  dz
                            y
                                                                 dy
                                         ρ  υ                               ∂( ρ  υ  )
                                          f  rf,x  dydz               ρ  υ rf,x +  f  rf,x
                                                                      f           dx dydz
                                                                              ∂x
                                      x
                         z
                   Figure 3.19 Balance of variables over the representative volume.
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