Page 264 - Membranes for Industrial Wastewater Recovery and Re-Use
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Case studies  2 3
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           Table 5.2  Specifications for water quality

           Parameter                                                 Maximum
                                                                     value
           Suspended solids (mg IF1)                                 <1
           Silt density index                                        <3
           Reovirus (100 ml-')                                       Nil
           Enterovirus (100 m1-l)                                    Nil
           Total coliforms (100 I&')                                 < 10
           Faecal coliforms (100 ml-I)                               <1
           Faecal streptococci (100 ml-l)                            <1



             Demineralising feed water has two requirements.  The first is that the water
           must  not contain  any  organic  matter  that  will  foul  the ion  exchange  resin,
           particularly  anion resin.  The  second  is that  the TDS  should  not  impose  any
           additional load  on the plant  over that of  domestic feedwater.  Benefits can be
           easily  obtained  if  the TDS  is in fact lower than the original supply  as it  can
           significantly  reduce  costs  through  fewer  regenerations  of  the  demineraliser
           plant. A prime requirement for all end uses, and one required by the New South
           Wales Environmental Protection Agency, is that the water be disinfected (Table
           5.2). A  number of  technologies  were considered  including ponding, wetlands
           and UV disinfection but all required additional treatment before the water was
           suitable for reuse at the plant and so membranes were ultimately used.


           5.2.2 Description of  plant
           Secondary effluent is supplied from the Dora Creek sewage treatment plant and is
           initially stored in a 8 M1 holding tank before being transferred to the treatment
           plant. The flow is supplied at a  rate of  3.5 M1 d-'  and blended  with  tertiary
           effluent from the station's sewage works and contaminated plant  water which
           has had  the oil and grit  removed.  The flow then passes  through a motorised
           screen before being pumped to the microfiltration plant (Fig. 5.3).
             Filtrate  from the MF plant  is dosed with sodium hypochlorite en route to a
           storage tank to control biological growth. Sulphuric acid (4%) is also added to
           reduce pH and minimise hydrolysis of  the RO membrane. Water is then pumped
           from the storage tank, dosed with anti-scalant, and screened through a  5 pm
           disposable cartridge filter before passing to the RO plant. Permeate is pumped to a
           degasser unit before being fed preferentially to the demineraliser plant because of
           its low TDS. The RO reject  stream is dosed with ferrous chloride before being
           passed to the station's ash dam together with waste from the demineraliser plant
           and the wastewater sump.

           Microfiltration
           The microfiltration plant incorporates two parallel streams each containing 90
           modules. Each module houses  15 m2 of  polypropylene hollow fibre membrane
           supplied  by  Memcor  and rated  at a  nominal pore  size of  0.2  pm.  The  plant
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