Page 385 -
P. 385

ION EXCHANGE APPLICATIONS IN WATER TREATMENT    12.43

         in  that  they  are  inherently  noncorrosive.  However,  they  are  not  available  in  very  large
         sizes  and are  generally  limited to  tank  diameters  of 8  ft and  less.  They  are  not generally
         used  for pressures  above  150  psig  or temperatures  above  100 ° F  (under pressure).  Steel
         tanks  can  be  made  in  almost  any  configuration.  However,  steel  tanks  are  heavier  than
         fiberglass tanks. They are almost always lined and, therefore, more expensive. Where high
         temperatures  are employed,  stainless  steel is  sometimes  preferred  over carbon  steel.  The
         cost of building a  stainless steel vessel makes  it prohibitively expensive for all but a few
         specialty  applications.


         Distributor  Design
        As  a bare minimum,  the tank  should be equipped  with  an inlet distributor, to get the wa-
        ter  into  the  tank,  and  an  underdrain  collector,  to  get  the  water  out  of  the  tank.  It is  ad-
         visable to have  if there  are  separate  connections for the introduction of the resin into the
        tank and the removal  of resin from  the tank.  For tanks  that are larger than  3  ft in diame-
        ter, it is necessary to have an access manway,  so that a worker  can  climb inside the tank
        to install or repair the internal distributors and collectors.  Manways  are best located at the
        top  of the  tank.  Larger  manways  are  preferable  to  small manways.  If the  manway  is  lo-
        cated on the side of the tank, it can create distribution problems.  View ports  are a feature
        used in more  sophisticated ion exchange  systems. They  allow  the operator to visually in-
         spect resin to  make  sure that resin has not been lost due  to  excessive  backwash  or prob-
        lems  with  the  underdrain  collector,  and  to  watch  the  resin  during  the  regeneration  and
        backwash  cycles  to  ensure that the resin bed remains packed  and does  not fluidize when
        it is not  supposed  to.
           To  ensure  the  proper  flow  of  liquid  through  the  resin  bed,  the  water  must  enter  the
        tank in such a  fashion as to provide minimum turbulence and laminar flow  into the resin
        bed.  Any protuberance will create a disturbance and an area of maldistribution. The resin
        bed  should present  a  flat surface  that the  water  can flow  straight down  through  and  into
        the underdrain collector. The path length should be equal for all portions of the bed.  Most
        pressure  vessels  have  dished heads.  The  dish  creates  a  disturbance that distorts  the flow
         and reduces  the  efficiency  of the  ion  exchange  resin.  Large  tanks  benefit from  the  addi-
         tion of either flat,  false bottoms  or subfills  such as  concrete  or  sometimes  gravel that fill
         the bottom head  and provide  a flat surface  for the resin bed to  lay upon.  By  far the most
         important factor in the efficiency  and quality produced  by  an ion exchange  system is the
         design of the internal distributors and collectors.  The inlet distribution system must allow
         the water and chemical to enter the vessel in such a way  as to spread out equally through-
         out the entire tank diameter with equal velocity.  The velocity must be sufficiently low  as
         to not disturb the resin bed below.  Distributor design is much  more  crucial in tanks  with
         limited freeboard. Underdrain collectors must be located as close to the bottom of the ves-
         sel  as  possible  with  the  least  amount  of  resin  underneath the  collector  as  possible,  and
         should have collection  spacing  of about 6  in.  Hub  and  lateral  collectors  have  a  problem
         in the  larger  tank  sizes  for two  reasons:  (1)  The  radials  are  far  apart  at  the  edges  of the
         tank. (2) The relative surface area close to the edge of the tank is large; however, the num-
         ber of collection points in a radial is small. Therefore,  it is very difficult in large tanks to
         get even distribution with the hub  and lateral design.  Another problem is that the hub  it-
         self causes  an  area  of poor distribution right in the center of the tank.
           If the underdrain  is  not  located  within  1 to  2  in.  of the  bottom  of the  tank,  the  rinse
         requirement  will  increase  significantly due  to  the  difficulty  of  removing  the  regenerant
         chemical that lays  out and hides below the collector.  The  underdrain must  also have  suf-
         ficient  open  area  to  collect the  water  without becoming  clogged  with resin.  The  slotted
         pipe  type  of  collectors  sometimes  used  in  the  less  expensive  and  smaller  systems  have
   380   381   382   383   384   385   386   387   388   389   390