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114   Analysis and Design of Energy Geostructures


                   The above indicates that the velocity field for an incompressible fluid is a solenoi-
                dal field, that is a field in which the divergence of the considered variable is equal to
                zero at all points in space.



                3.12.3 Laplace’s equation
                Recalling that Darcy’s law expresses a relationship between the seepage velocity and
                the hydraulic gradient, Eq. (3.42) can be rewritten as
                                                r  krhÞ 5 0                           ð3:43Þ
                                                   ð
                   Assuming the medium to be isotropic allows the writing of the following form of
                Laplace’s equation (e.g. for the piezometric head)
                                                   2
                                                  r h 5 0                             ð3:44Þ
                                2
                   The quantity r h is as follows in various coordinate systems.
                •  Cartesian coordinates x, y, z:
                                                   2      2     2
                                              2
                                            r h 5  @ h  1  @ h  1  @ h                ð3:45Þ
                                                    2      2     2
                                                  @x     @y    @z
                •  Cylindrical coordinates r, θ, z:

                                               2              2     2
                                         2
                                        r h 5  @ h  1  1 @h  1  1 @ h  1  @ h         ð3:46Þ
                                                            2
                                                2          r @θ 2    2
                                              @r    r @r           @z
                •  Spherical coordinates r, θ, φ:
                                      2             1   @               1    2
                                2
                               r h 5  @ h  1  2 @h  1      sinθ  @h  1      @ h       ð3:47Þ
                                                                          2
                                       2          r sinθ @θ    @θ     r sin θ @φ 2
                                                                      2
                                                   2
                                     @r    r @r
                   Eq. (3.44) is associated with steady-state conditions and often represents the basis
                for analysis and design considerations.

                3.13 Initial and boundary conditions for mass conservation

                Analogous considerations to those presented for characterising heat transfer problems
                hold for describing mass transfer problems with reference to the initial and boundary
                conditions. In this case, the boundary conditions are generally expressed either as a
                function of a hydraulic head, H (Dirichlet’s condition) or a flux, @H=@n i (Neumann’s
                condition).
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