Page 223 - Hydrogeology Principles and Practice
P. 223

HYDC06  12/5/05  5:33 PM  Page 206






                 206    Chapter Six


                                                               Combining the mathematical description of
                                                             mechanical dispersion with the molecular diffusion
                                                             coefficient gives an expression for the hydrodynamic
                                                             dispersion coefficient, D, as follows:

                                                             D = α V + D*
                                                              l   l l
                                                                                                 eq. 6.6
                                                             D = α V + D*
                                                              t   t t
                                                             where the subscripts  and  indicate the longitudinal
                                                                              l   t
                                                             and transverse directions, respectively.
                                                               The relative effects of mechanical dispersion
                                                             and molecular diffusion can be demonstrated from
                                                             the results of a controlled column experiment. The
                                                             breakthrough curve for a continuous supply of tracer
                                                             fed into a column packed with granular material is
                                                             shown in Fig. 6.7. At low tracer velocity, molecular
                                                             diffusion is the important contributor to hydrodyn-
                                                             amic dispersion, although with little effect in spread-
                                                             ing the tracer front. At high velocity, mechanical
                                                             dispersion dominates and the breakthrough curve
                                                             adopts a characteristic S-shape with some of the
                                                             tracer moving ahead of the advancing front and
                                                             some lagging behind, as controlled by the tortuosity
                                                             of the flowpaths. The midpoint of the breakthrough
                                                             curve occurs for a relative concentration, C/C , equal
                                                                                                0
                                                             to one-half. This point of half-concentration repres-
                                                             ents the advective behaviour of the solute transport
                                                             (shown by the vertical dashed line in Fig. 6.7) as if the
                                                             tracer were moving by a plug-flow-type mechanism.


                                                             One-dimensional solute transport equation
                                                             Following from the above description of solute
                                                             transport processes, the one-dimensional form of the
                                                             solute transport equation describing the time-varying
                                                             change in concentration of non-reactive dissolved
                                                             contaminants in saturated, homogeneous, isotropic
                                                             material under steady-state, uniform flow conditions




                                                             Fig. 6.6 (left) Results of a tracer experiment in the Cape Cod sand
                                                             and gravel aquifer showing: (a) the distributions of relative
                                                                              −
                                                             concentrations (C/C ) of Br observed 13 and 83 days after
                                                                          0
                                                             injection (dashed where inferred); (b) calculated longitudinal
                                                                        −
                                                             variances of the Br tracer plume for each synoptic sampling
                                                             round. Also shown in (a) are locations of multilevel samplers
                                                             available for groundwater sampling (solid circles) and tracer
                                                             injection (solid squares). After Hess et al. (2002).
   218   219   220   221   222   223   224   225   226   227   228