Page 48 - Membranes for Industrial Wastewater Recovery and Re-Use
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28  Membranesfor Industrial Wastewater Recovery and Re-use













            Pressurized
            F



                                          '..
                            ~


            Figure 2.9  Spiral-wound module, schematic showingflow streams (by kingpermission oflonics)

         linking the retentate streams in series and placing the module in an appropriate
         pressure vessel.
           Tubular modules provide a modest surface area to volume ratio, and thus the
         highest  cost  per  unit  area  of  all  cylindrical membrane  geometries, but  also
         provide potentially the greatest turbulence promotion and the best access to the
         membrane  surface.  Both  these  factors  tend  to  favour  this  configuration  for
         highly fouling matrices. If the tube diameter is sufficiently large it is possible to
         mechanically clean the membranes in place, as is carried out with the FYNEOZ;
         nanofiltration process developed by PCI Membranes. This process uses foam balls
         to wipe the inner surface of  the membrane tubes once fouled, thus minimising
         the use of  chemicals for this duty. Commercially available modules are mainly
         multi-channel (Fig. 2. lo), with mechanical support required for the polymeric
         tubes.  The ceramic  tubes tend  to  have  a lower packing  density  due to  their
         monolith  construction: the tubes comprise cylindrical holes bored into a solid
         ceramic support. The brittle nature of the ceramic material imposes a lower limit
         on the tube wall thickness, tending to increase the overall membrane hydraulic
         resistance over that of a comparable polymeric membrane.
           The inherent radial mechanical strength of  a tube increases with decreasing
         diameter, such that at a certain diameter the tube becomes self-supporting. This
         is the case for capillary tubes and hollow fibres. The highest packing densities are
         obtained from hollow fibre membrane modules (Fig. 2.11). These can have inner
         diameters as small as 10 pm for particularly fine fibres (hence hollow fine fibres,
         or HFF), which therefore give the highest packing densities and so the lowest
         cost. The module is of a very simple construction. The bundle of fibres is simply
         bent double and the ends potted and exposed at one end of  the tube into which
         they are inserted. Hollow fibre modules operate out-to-in, such that the skin is
         formed on  the  outer  membrane surface.  Capillary fibres modules, which  are
         slightly larger filaments, are operated in-to-out with the skin therefore formed on
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