Page 266 - Membranes for Industrial Wastewater Recovery and Re-Use
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Case studies  2 3 5



















             Figitre 5.4  (a) Microfiltratiori arid (b) reverse nsriiosispilotplarits at Eraririgpoa~erstcitiori

        5.2.3 Performance
        The  plant  is  reported  to  have  performed  well  since  its  installation and  has
        resulted in significant water savings. The percentage  of  reclaimed  water used
        has increased gradually from 5.2% during installation in 1994 to 56.7%) in 1998
        such that up to February 1999 the plant has used a total of 2 3 3 3 M1 of reclaimed
        water. In 1999, potable water use at the site was 1.8 M1 d-'  and this is expected
        to be ultimately reduced to 400 kl d-l  by 2010 when the duration of the deed of
        agreement is complete.
          The treatment performance is indicated by a reduction in BOD  from 20 to 50
        to  less  than  1 mg 1-'  across  the  whole  plant  (Table  5.20). The  equivalent
        removal for turbidity  is from  50 to  <0.1 NTU  and for Faecal coliforms  from
         < 10'  to  < 1. RO  permeate  is  also  low  in  dissolved  solids  with  a  permeate
        concentration of specific ions of  32 mg 1-'  (Cl), 2.2 mg 1-1  (Si), 17.8 mg 1-'  (Na)
        and  0.5  mg 1-'   (Ca).  The  low  levels  of  dissolved  solids  have  increased
        demineraliser cation operation  capacity from  2 176 m3 with potable  water to
        4792 m3 with reuse water and anion operation capacity from 2113 m3 to 3472
        m  respectively before requiring a regeneration.
          The main  operational concerns  have been  periods  of  increased  membrane
        fouling. At one stage the MF plant  was not responding  to the cleaning cycle.
        Diagnosis  revealed  manganese fouling  was  occurring which  was  completely
        ameliorated  with  a  citric  acid  (citriclean) clean.  Similarly,  at  one  stage  RO
        cleaning frequency increased dramatically. The problem was linked to organic
        fouling which decreased naturally as indicated by reduced chlorine demand and
        ammonia levels in the plant. Ifthe problem occurs again a chlorine chemical clean
        is planned to oxidise the organic layer. An important aspect of the scheme has
        been gaining employee acceptance of using reclaimed water. To allay fears and
        concerns  regular  testing  for  bacteria  and  viruses  is  reported  and  personal
        protective equipment (ppe) and covers for equipment is supplied were appropriate.
          The  water  reclamation  plant  originally  required  a  total  capital  cost  of
        AUD$4.5 million($3.34million)in 1994ofwhichAUD$4million (S2.96million)
        was construction and commissioning and AUD$0.5 million ($0.3 7 million) was
        required  for  segregating  the potable  and reclaimed  water supplies.  A further
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