Page 141 - Membranes for Industrial Wastewater Recovery and Re-Use
P. 141

Industrial  waters  11 5


           chemicals  can  interfere  with  the  sensitive  chemical  equilibrium  in  the  wet
           processing.
             Suspended solids-free process water or effluent is not always sufficiently clean
           for recycling purposes. When the freshwater consumption is reduced the water
           circulation system becomes enriched in dissolved and colloidal substances (DCS),
           which causes several problems within the process operation and/or in the paper
           product. High levels of dissolved organics result in enhanced bacterial growth in
           the  system,  possibly  producing  odour  problems  in  the  paper  product  and
           increasing  BOD  and  colour  levels  in  the  effluent  streams.  Enrichment  of
           multivalent ions also produces problems of scaling (carbonates and silicates) and
           corrosion  (sulphates, chlorides,  Fe2+ and  A13+) which  tend  to  arise  after
           extended periods  of  operation  under  conditions  of  low  freshwater  use.  Also,
           brightness  reversion  can be caused  by  dissolved inorganic materials  such as
           Fe2+. Problems  of  enrichment of  the DCS  in the white  water  system  can be
           substantially  ameliorated  through  advanced  purification  methods,  such  as
           ultrafiltration (UF), as will be shown later.
             The stress imposed on water resources has forced the mills to seek ways to
           efficiently treat their effluents to freshwater quality levels of purity. For example,
           the  total  mill  effluents  treated  by  biological  and  membrane  processes
           (Bentley,1999; Webb,  1999) or  evaporation  (Stevenson,  1992) have  been
           successfully  used to supplement freshwater  supplies. However, coating colour
           effluents have proved  problematic  to treat because they are not degraded  by
           biological  processes and, as a  result  of  this, chemical precipitation  has been
           widely employed. This produces a solid waste that must be landfilled. During the
           1990s concentration of  coating colour effluents by UF  became more common,
           mainly for economic reasons: UF costs have decreased whereas landfill disposal
           costs have increased. In the IPPC directive UF treatment of  the coating colour
           effluents is now stated as a BAT technology.


           3.2.5 Membranes  in the pulp and paper industry
           There has been increased interest in membrane filtration applications in the pulp
           and paper industry over the last 15-20 years, for reasons already stated above as
           well as in Section 1. Membrane processes offer a high level of purification coupled
           with a low footprint and relatively low energy consumption, especially when
           compared with the competing desalination technology of evaporation.

           Existing full-scale membrane plants
           The first full-scale reverse osmosis plant was installed in the white water system
           of  a board machine of Green Bay Packaging Inc. in the USA in 19 74 (Macleod,
           1974). Later when the water balance  of  the board  machine changed the RO
           plant became redundant. Since the 1980s tubular module ultrafilters have been
           successfully  adopted  for such purposes  as concentration and fractionation  of
           spent sulphite liquor (Anon., 1982; PCIMembrane Systems, 1988), deresination
           (Paterson Candy,  1987) and bleaching effluent treatment (Haagensen, 1982:
           Okamoto et al., 1985; Jonsson, 1987; Wickstrom, 1997). An early example of
   136   137   138   139   140   141   142   143   144   145   146