131
        
        
          Honour Lectures /
        
        
          
            Conférences honorifiques
          
        
        
          5
        
        
          0
        
        
          1
        
        
          2
        
        
          3
        
        
          4
        
        
          5
        
        
          6
        
        
          0 0.2 0.4 0.6 0.8 1
        
        
          (b )
        
        
          Depth (m)
        
        
          R elative C oncen tration,
        
        
          
            C
          
        
        
          (
        
        
          
            x
          
        
        
          ,
        
        
          
            t
          
        
        
          )/
        
        
          
            C
          
        
        
          
            o
          
        
        
          
            k
          
        
        
          
            h
          
        
        
          = 10
        
        
          -8
        
        
          m /s
        
        
          P ure
        
        
          A dvection
        
        
          A dvectio n
        
        
          +
        
        
          M echanical
        
        
          D ispersion
        
        
          A dvection
        
        
          +
        
        
          Diffusio n
        
        
          0
        
        
          1
        
        
          2
        
        
          3
        
        
          4
        
        
          5
        
        
          6
        
        
          0 0.2 0 .4 0.6 0 .8 1
        
        
          (c )
        
        
          Depth (m)
        
        
          R e lative C o ncen tration ,
        
        
          
            C
          
        
        
          (
        
        
          
            x
          
        
        
          ,
        
        
          
            t
          
        
        
          )/
        
        
          
            C
          
        
        
          
            o
          
        
        
          
            k
          
        
        
          
            h
          
        
        
          = 1 0
        
        
          -9
        
        
          m /s
        
        
          P ure
        
        
          A dvectio n
        
        
          A dvectio n
        
        
          +
        
        
          M ec ha nica l
        
        
          D isp ers io n
        
        
          A dvectio n
        
        
          +
        
        
          D iffusio n
        
        
          0
        
        
          1
        
        
          2
        
        
          3
        
        
          4
        
        
          5
        
        
          6
        
        
          0 0 .2 0 .4 0 .6 0 .8 1
        
        
          (d )
        
        
          Depth (m)
        
        
          R e la tiv e C o n c e n tra tio n ,
        
        
          
            C
          
        
        
          (
        
        
          
            x
          
        
        
          ,
        
        
          
            t
          
        
        
          )/
        
        
          
            C
          
        
        
          
            o
          
        
        
          
            k
          
        
        
          
            h
          
        
        
          = 1 0
        
        
          -10
        
        
          m /s
        
        
          P u re
        
        
          A d v e c tio n
        
        
          A d v e c tio n
        
        
          +
        
        
          M e c h a n ic a l
        
        
          D is p e rs io n
        
        
          A d v e c tio n
        
        
          +
        
        
          D iffu s io n
        
        
          Figure 2. Representative concentration profiles beneath a ponded
        
        
          source of liquid after an elapsed time of 5 yr: (a) schematic of
        
        
          scenario (
        
        
          
            n
          
        
        
          = 0.5,
        
        
          
            D
          
        
        
          
            *
          
        
        
          = 6 x 10
        
        
          -10
        
        
          m
        
        
          2
        
        
          /s,
        
        
          
            i
          
        
        
          
            h
          
        
        
          = 1.33); (b) advective
        
        
          dominated case; (c) diffusive significant case; (d) diffusive
        
        
          dominated case.
        
        
          The most common scenario is illustrated in Fig. 3b,
        
        
          where both hydraulic and concentration gradients act in the
        
        
          same direction to drive advective and diffusive chemical
        
        
          transport from the containment side of the barrier to the
        
        
          surrounding medium. This scenario also is the scenario
        
        
          depicted previously with respect to Figs. 1 and 2.
        
        
          Figure 3. Transport scenarios across horizontal barriers for waste
        
        
          containment: (a) pure diffusion; (b) diffusion with positive
        
        
          (outward) advection; (c) diffusion with negative (inward)
        
        
          advection (modified after Shackelford 1989, 1993).
        
        
          The third scenario (Fig. 3c) pertains to the case where
        
        
          the hydraulic and concentration gradients act in opposite
        
        
          directions, such that advective transport is directed inward
        
        
          towards the containment side of the barrier, whereas
        
        
          diffusive transport still is directed outward. As a result, the
        
        
          net outward advance of the chemicals is slowed or
        
        
          "retarded" by the opposing hydraulically driven transport.
        
        
          This situation would arise, for example, when the
        
        
          containment system is located at a site with a high
        
        
          groundwater table, such as a perched water table, such that
        
        
          the barrier is located below the water table. This scenario
        
        
          has been referred to as "zone of saturation" containment
        
        
          (e.g. Shackelford 1989, 1993). The scenario also has been
        
        
          referred to as a "hydraulic trap," because the inward
        
        
          directed hydraulic gradient enhances the containment
        
        
          function (e.g., Rowe et al. 2000, Badv and Abdolalizadeh
        
        
          2004). However, because diffusion is still prevalent, the
        
        
          existence of an opposing hydraulic gradient does not
        
        
          necessarily mean that no contaminant will escape
        
        
          containment, as the net effect will depend on the
        
        
          magnitude of advective transport relative to that for
        
        
          diffusive transport. Also, the effectiveness of inward
        
        
          gradient landfills may not be as complete as expected in
        
        
          the case where the barrier possesses semipermeable
        
        
          membrane properties (Whitworth and Ghazifard 2009).
        
        
          4.2
        
        
          
            Diffusion through Barriers or Barrier Components
          
        
        
          4.2.1
        
        
          
            Diffusion in Natural Clays
          
        
        
          The recognition that diffusion may play an important role
        
        
          in governing contaminant migration gained momentum in
        
        
          the late 1970s with the publication of a case study by
        
        
          Goodall and Quigley (1977) describing the field
        
        
          concentration profiles that existed beneath two landfill
        
        
          sites near Sarnia, Ontario, Canada, viz. the Confederation
        
        
          Road landfill and the Blackwell Road landfill. The pore
        
        
          water obtained from Shelby tube samples collected beneath
        
        
          a landfill sited directly on top of intact glacial till, and the