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244  Membranesfor Industrial Wastewater Recovery and Re-use


          of 40 000 m3. The internal heating loop has reduced gas consumption by 20%
          from  660 m3 tor1 to  520 m3 ton-l  producing  an overall  saving  in  gas of
          700000  m3. Total  wastewater  discharged  from  the  sites  has  halved  to  a
          population equivalent of  5000 p.e. which generates a saving of €22 7 000 per
          year ($226 000).



          5.5  Kronospan  Ltd:  medium-density  fibreboard  wash  water
          recycling (UK)



          5.5.1 Background
          The production of medium-density fibreboard (MDF) involves a number of simple
          but large-scale  operations. Forest thinning and sawmill residues are debarked
          and chipped before being washed to remove residual dirt and grit from the wood.
          The fibres are then steam-softened, cooked and refined between two flat plates
          and finally mixed with resin to produce the fibreboard.
            An  example  facility  is  at  Chirk  in  North  Wales  where  Kronospan  UK
          manufacture  chipboard,  MDF, melamine-faced  boards  and sawn timber. The
          plant produces  47800 m3 of  MDF  effluent  per  year  of  which the majority is
          associated with the washing and refining stages of  production. The quantity of
          excess water generated during the process depends on the moisture content of
          the wood and can range from 400 1 per tonne of bone dry wood processed in the
          summer to up to 600 1 in the winter. The characteristics of the effluent are high
          COD and high suspended solids of which cellulose, lignins and resin acids are key
          components.
            Prior  to  1995 the effluent  was  tankered  off  site at a  cost  of  €9.8 tonne-l
          ($14.72  tonne-').  The company  was  not only  concerned  about the cost  of
          this option but also the risk to production  if the tankers failed to arrive as the
          site could only  store one day's  effluent.  A  decision was made  to incorporate
          on-site  treatment  at the production  facility which should meet the following
          aims:

            0  Low capital cost/rapid investment payback
            0  Optimum productfresource recovery
            0  Effluent reduction, recycling and reuse
            0  Long-term environmental compliance
            0  Easy to upgrade modular system

            The  site  contained  an  existing  conventional  biological  treatment  train
          comprising a dissolved air flotation unit followed by an activated sludge plant.
          Problems with effluent reliability and limited resource recovery due to the poor
          effluent  quality  led  to  the  search for  an  alternative solution.  Ultimately,  a
          treatment  train  containing  membranes was  installed  in June  1995, which
          offered the potential for zero discharge of the wash water effluent.
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