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88  Mrmbranes for lndustrial Wastewater Recovery and Re-use




           The extent of  recirculation  can be increased by  using  chemical treatments
         either to  adjust  the  pH  of  the  water  or  to  sequester  minerals  and  prevent
         deposition, in the same way as reagents are used to ameliorate scaling in reverse
         osmosis plant (Table 2.15). In most cases, the Rc is optimised based  on water
         availability,  water  quality,  and  treatment  costs.  Typically,  evaporative
         recirculating  cooling towers that use reclaimed  water operate with Rc values
         ranging from 1 to 3. An advantage of higher Rc values is that reduced quantities
         of make-up water are required and there is less blowdown water to be treated or
         discharged. It should be noted that the concentration of dissolved constituents in
         the blowdown  water  increases  with  increasing  Rc.  Therefore,  one  trade-off
         associated with higher Rc levels is the increasing costs of disposal or treatment of
         the blowdown water.
           The impact of recirculation on water quality in a recirculating cooling system
         using reclaimed water as a source water is shown in Fig. 3.11. This system is
         operated with a Rc of  about 2. A comparison of the conductivity of  the source
         water  to  that  of  the  recirculating  stream  reveals  that  the  concentration  of
         dissolved solids increases about two-fold in this system. When blowdown water
         is removed from this system it is returned to the wastewater reclamation facility.
         Higher Rc values for this source would yield a blowdown water with a higher salt
         content that might preclude discharge to the wastewater reclamation facility.


         3.1.7 Cooling tower water quality issues
         Industrial  cooling  tower  operations  are  susceptible  to  four  potential  water
         quality  problems:  (1) scaling,  (2) biological  growth, (3) fouling  of  the  heat


                5000  1

             5  4000
             a
             3.
             .&  3000
                                                          Cooling Water
             .L
                2000
             3
             W
             C
             6  1000

                   0’
                   Jan-00    Jul-00   DeoOO      Jun-01   Dec-01    Jun-02
                                              Date
         Figurr 3. I1  Comparison of  the conductivity of  source ivater and rrcirculatrd  wntrrfor n cooling systrm
         operatrd by Rnythron Corporationin St. Petersburg, Floridn (Knighton, 2002)
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