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154  Membranes for Industrial Wastewater Recovery and Re-use


          retain the dissolved chemicals whilst removing colour down to very low levels.
          Ultrafiltration membrane processes allow selective recovery of sparingly soluble
          dyes, such as indigo, but downstream reverse osmosis is then usually required to
          remove soluble dyes  (Cheryan, 1998; Woerner  et al.,  1996; Marcucci et a].,
          2001; Sojka-Ledakowicza et al., 1998). Having said this, some interesting results
          have been reported by Porter and his various co-workers whereby low molecular
          weight anionic dyes were found to be substantially rejected by a titanium dioxide
          microfiltration membrane (Zhang, 1996; Porter and Gomes, 2000). This was
          attributed  to  charge  rejection,  and  charged  UF  membranes  have  been
          successfully employed in  South  Africa  for  selectively recovering  water  and
          dissolved salts (Erswell  et al., 1988).
            Most  operating  membrane-based  dyewaste  recovery  and  reuse  systems
          ultimately make use of reverse osmosis or nanofiltration to decolourise. Payback
          periods are invariably long even where freshwater costs are high, although two
          bench-scale studies have reported calculated  operating costs of  between $0.5
          and $1 per m3 product (Voigt et a]., 2001; Ciardelli et al., 2001). For two South
          Africa installations the payback ranges from just less than three years for an NF
          process (Buckley, 1992), to over seven years for a system combining ceramic UF
          with RO (Short, 1993). A payback period of  1.37 years was quoted for a UF/NF
          plant in North Carolina (NCDENR, 1995), although no further detail was given.
          Given the continuing downward pressure on membrane costs, the increasing
          stringency  of  environmental  regulations  worldwide  and  the  history  of  the
          employment of  membranes for textile wastewater treatment  and recycling in
          certain regions of  the world, and South Africa in particular, it seems inevitable
          that the use of membranes for this duty will become more widespread in years to
          come.



          References
          Allen, W., Prescott, W.B., Derby Jr, R.E., Garland, C.E., Peret, J.M. and Saltzman,
          M. (1 9 72). Determination of  color of  water and wastewater by means of  ADMI
          color values. Proc. 28th Ind. Waste Conf., Purdue University, Lafayette, IN, pp.
          661-6  75.
            Akbari. A,, Desclaux, S., Remigy, J.C.  and Aptel, P.  (2002). Treatment  of
          textile  dye  effluents  using  a  new  photografted  nanofiltration  membrane.
          Desalination, 149,101-10 7.
            Bal,  AS.,  Malewar.  C.G.  and  Vaidya,  A.N.  (1991). Development  of  non-
          cellulosic membranes for wastewater treatment. Desalination, 83,32 5-3  30.
            Bennett, A.R.  (2000). Recovery of wool scouring effluent utilising membrane
          bioreactor (MBR) technology as part of  the activated sludge system followed by
          two-stage  reverse  osmosis  (RO)  membrane  concentration.  In  Hillis, P.  (ed.)
          Membrane  technology  in  water  and  wastewater  treatment,  Specialist
          publication 249, RSC, pp. 219-225.
            Bes-Pia, A., Mendoza-Roca, J.A., Alcaina-Miranda, M.I.,  Iborra-Clar, A. and
          Iborra-Clar, M.I. (2002). Reuse of  wastewater of  the textile industry after its
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