Page 276 - Membranes for Industrial Wastewater Recovery and Re-Use
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Case studies  245


         55.2 Description of  plant
          The  effluent  treatment  plant  treats  all  the  MDF  effluent  generated  within
          the production facility. Excess flow is stored prior to it being pumped  into the
          treatment  plant.  The  plant  consists  of  multiple  treatment  stages  combining
          physicochemical  processes  with  membrane  technology  (Fig.  5.10).  Water
          entering the plant is initially dosed with a polyelectrolyte  and flocculated. The
         flocculated suspension is then pumped  into a plate and frame filter press from
         which a 45-50%  dry solids cake is recovered. The filter cake can be burnt in the
         boiler or re-used  in chipboard  production. The filtrate passes through a  dual
         media depth filter before entering a four-stage reverse osmosis plant. Permeate
         from the membrane plant is polished through an activated  carbon bed before
         being reused  on site for boiler feed. Concentrate from the membrane plant  is
         returned  to the resin make up tank and backflush/wash  water from the sand
         filter and filter press  are combined  and returned  to the head of  the treatment
         works.

         Pretreatment
         Polyelectrolyte  is  dosed  up  to  a  rate  of  500 mg 1-1  into  the  flow  and  then
         flocculated in a 15 m3 tank with a residence time of 30 min. The project included
         the development of  a new polyelectrolyte  specifically designed for the needs of
         MDF effluent. The flocculated suspension then passes to a 55-plate filter press at
         up to 50 m3 h-'  and 6 bar (treating an average flow of  30 m3 h-l). The press
         (Fig. 5.11a) produces up to 2 m3 of  45-50%  solids cake per batch. Filtrate from
         filter  press  then  passes  to  a  dual  media  depth  filter  containing  sand  and
         anthracite. The filter operates at a design velocity of  6 m3 m2 h-l  and requires
         cleaning with a combined air scour and water backwash which results in a water






                                                               Multimedla
                                                               depth filter
                                         Waste heat boiler
                       Carbon  ,-,                          PrOduCtiOn





                       finer
                                             Concentrate
                            ~
                                                   Process water main
                                    Treated water
                                      tank
                 Figure 5. IO  Processflow diagram for Kronospan zero discharge and recovery plant
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