Page 191 - Membranes for Industrial Wastewater Recovery and Re-Use
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160  Membranes for Industrial Wastewater Recovery and Re-use


            Several systems have been used to recycle this water, with various degrees of
          water  product  purity.  Filtration,  pH  adjustment  and  chlorination does  not
          address  the  high  TDS  and  demands  a  constant  bleed:  the  treated  water
          quality  does  not  meet  potable  guidelines  and  consequently  this  system  has
          only  been  used  in  the  event  of  severe  water  shortages.  Carbon  dioxide
          addition,  dealkalisation  by  ion  exchange and  UV  sterilisation  represents  an
          improvement  over  filtration-based  methods  and  has  been  implemented  in
          some German facilities. Filtration followed by pH correction and reverse osmosis
          has been  used  only in very few installations  because of  the high capital  and
          operating cost, and can only be justified where both the water and effluent costs
          are high.
            In the majority of  cases the water from the final rinse can be used virtually
          untreated in applications such as crate washers and as pasteuriser make-up after
          cooling.  In  addition  the water  can be  collected  and used  for  floor  washing.
          Because  the cost of  treatment in these cases is negligible, most of  the reclaim
          applications adopt these procedures.
            A recent example of water recycling and reuse is at the Coca Cola Amatil plant
          in  New  South Wales  (Environment  Australia,  2001). Two  simple  recycling
          initiatives have been  undertaken at this plant, the first involving reuse of  the
          backwash water and the second the reuse of container rinse water. Interestingly,
          the first  of  these,  which  recovers  around  200 m3 day-'  of  backwash  water
          from the sand and carbon filters, appears to be blended with the mains water and
          reused in the manufacturing process. The blend is maintained at less than 1:5
          recovered:mains  water.  The  payback  time  for  the  recycling  system,  which
          comprises pipework  and a  backwash  water recovery  tank, is estimated  to be
          around two years.  The recovered container rinse water, on the other hand, is
          used in the evaporative cooling towers following filtration. About  16 m3 day-l
          is recovered for this duty.

           Caustic recovery
          In the majority of food and beverage applications a large amount of caustic soda
          is used for bottle washing and CIP (clean in place) applications. The disposal of
          the  spent caustic  solution  is  problematic  and  expensive.  In  most  cases  the
          effectiveness  of  the  caustic  solution  is  assessed  by  assaying  for  carbonate
          contamination  or  dirt  content: when  these  levels  reach  a  certain  limit  the
          solution is disposed of. The caustic content may still be quite high, however, and
          nanofiltration  membranes have been  developed  (Koch and PCI  Memtech) to
          clean and concentrate the spent caustic solution. The process plant for this duty
          is quite expensive, and the economics are such that the plant is only justified if
          the caustic volume used and cost of its disposal are both very high.

          Bottle or can pasteurisers
          An improperly balanced pasteuriser can use a large amounts of  water which is
          often discharged direct to drain. In most cases this water can be recycled back to
          the pasteuriser  directly  after  cooling and filtration.  Checks must be made  on
          product contamination in the case of bottle pasteurisers.
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