Page 188 -
P. 188

HIGH-RATE GRANULAR MEDIA FILTRATION           8.7

         pores become  rapidly  plugged,  and carbon  life is quickly reduced.  If turbidity,  taste,  and
         odor are  all significant problems,  GAC  beds  should be preceded  by  conventional  granu-
         lar media filtration. If carbon  adsorption  is desired to remove organics,  the depth of GAC
         that can be provided in a converted gravity filter is likely to be too shallow to provide ad-
         equate  contact  time;  however,  this  may  offer some  additional  carbon  removal after con-
         ventional  sedimentation.
         Uniform Media.   Uniformly  graded  deep-bed  filters  use  relatively coarse  media,  rang-
         ing  from  0.5  mm  to  as  much  as  6.0  mm.  The  UC  is  typically  1.2  to  1.3,  but  values  as
         high  as  1.5  may  be  found.  Greater  media  depth  is  substituted  for the  lack of fine  media
         in  the  bed.  Such  a  substitution  requires  more  vigilant operation  of pretreatment  systems
         to avoid breakthrough.  Depths  of 4  to 6  ft (l.2  to  1.8 m)  are common,  and  in some cases
         media  depths  reach  8  ft (2.4  m).  Filters  of this  type  are  not expanded  during  backwash,
         and  stratification of grain sizes does not occur. These filters are generally designed to use
         air or air/water backwash.
           There are many possible  combinations  of filter media size d  and depth L.  J. M. Mont-
         gomery (1985) presents a methodology for determining the optimum relationship between
        these two variables. The relationship between L and ES de (10%  finer) of many high-rate
        filters  is  shown  in  Figure  8.1.  In this  figure,  the  average  ES  for a  dual-  or mixed-media

                             Approximate average media grain size (d),  mm
                     O.l   0.3   0.5   0.8   1.0   1.3   1.5   1.8   2.0
             1.5  x  10 `3
                                                   f=
                                                  O. 50(
             1.3  x  103                                            4.0
                                                 0.475--
                                              t~
                                     &    •
             1.0  x  103
                                                                    3.0
           E
                              Conventional
           E
                                 filters
                              (150  m/d  max.)
              8x102
                                                                       .m_
                                   o   o  c
                                                                       E
                                  o  o~,,~
           E
                                                                    2.0
                                O  O
                                                                       iZ
           L~
              5x102
                                rl          "f  Sand filter for WTP
                                                                    1.0
              3x102
                                °  o   o   o   li•  Reverse graded filter for WTP
                                              Direct filtration filter
                                 Hardinge     Tertiary filter for WWTP
                                 filters
                  OL
                    0       0.3   0.5       0.8    1.0      1.3   1.5
                               Effective size of media grain (de),  mm*
                   *Weighted average to be used for dual  or multimedia  bed
          FIGURE 8.1  Relationship between depth and size of media. (Courtesy of MWH Americas Inc.)
   183   184   185   186   187   188   189   190   191   192   193