Page 50 - Membranes for Industrial Wastewater Recovery and Re-Use
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30  Membranes for Industrial Wastewater Recovery and Re-use

        manufacture.  Hence,  some  companies  have  started  producing  cassettes
        alongside their pressure-sealed module products.
          One  noteworthy  recently  development  concerns  ceramic  membranes.  As
        already stated, the onus is on suppliers of  these membranes  to reduce costs to
        make them economically competitive with the much less expensive polymeric
        materials.  It  appears  that  this  might  be  achievable  by  extruding  ceramic
        membrane substrates to produce channels of  rectangular geometry (Fig. 2.12).
        The cost of these membranes, produced from silicon carbide substrate monolith
        coated  with  titania, alumina or zirconia,  can be  as low  as $100 per  m2 for
        narrow-membrane channels (2 mm).
          Another  fairly  recent  development  is  the  use  of  aeration  combined  with
        submerged membrane  systems. Submerged  (or immersed) membrane systems,
        where large-area membrane filtration modules are submerged in a tank and the
        permeate  removed  at  very  low  transmembrane  pressures,  were  originally
        developed  for  membrane  bioreactors  (MBRs) by  companies  like  Kubota  and
        Zenon in the late 1980s as an alternative to the more conventional sidestream
        (or external) filtration systems. MBRs are an example of a hybrid process, in this
        case  combining  the  activated  sludge  aerobic  biotreatment  process  with
        membrane filtration (Stephenson et al., 2000). The high fouling propensity of the
        sludge liquor being filtered, which can have a suspended concentration of  up to
        20 g lP1, demands a high degree of turbulence promotion to enhance the flux. In
        the  submerged  system  turbulence  promotion  is  provided  by  coarse  bubble
        aeration. It has been shown by a number of  researchers (Ghosh and Cui, 1999;
        Mercier et al.,  1997; Cabassud et al.,  1997) that air-water  two-phase flow can
        substantially enhance the membrane  flux over  that attained  by  single-phase






























              Figure 2.12  Cerameni silicon carbide monolith substrate (reproduced withpermission)
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