Page 29 - Membranes for Industrial Wastewater Recovery and Re-Use
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lntroduction  9


           Table 1.6  Membrane processes
           Process                    Usual objective
           Microfiltration (MF)       Removal of suspended solids, including microorganisms
           Ultrafiltration (UP)       Removal of both large, dissolved solute molecules and
                                      suspended colloidal particles
           Nanofiltration (NF)        (Selective) removal of multivalent ions and certain charged  or
                                      polar molecules
           Reverse osmosis (RO)       Removal of inorganic ions
           Electrodialysis (ED) and dialysis   (Selective) extraction  of ions from water and/or
                                      concentration
                                      of these ions in the waste stream
           Pervaporation (PV)         (Selective) extraction of molecular gas and/or volatile solutes
           Gas transfer (GT)          Transfer of molecular gas into or out of water


             1.  Separation is achieved without requiring a phase change, and is therefore
           more energetically efficient than distillation.
             2.  Little or no accumulation takes place in the process which therefore operates
           continuously  under  steady-state  condition  without  necessitating  regeneration
           cycles, unlike adsorptive separation processes.
             3.  Little or no chemical addition is required, unlike conventional clarification
           which generally relies on the addition of chemical coagulants and flocculants.

             Membrane  technology  development  as  a  whole  began  with  the first  high-
           performance reverse osmosis membrane produced by in the early 1960s (Loeb
           and  Sourirajan,  19631,  which  led  to  the  installation  of  large  seawater
           desalination plant in arid regions of the world. Since that time, growth in the
           total quantity of membranes sold with reference to the water treatment capacity
           provided has increased exponentially with time, with growth in microfiltration
           and ultrafiltration  technologies  over the last decade of  the twentieth century
           being  particularly  pronounced  (Fig.  1.1). There  has  been  a  corresponding
           exponential  decrease  in  membrane  costs  with  installed  membrane  plant
           capacity,  as reflected  in data from  an established  hollow fibre microfiltration
           membrane  (Fig.  1.2). The  increasing  stringency  of  water  quality guidelines
           and standards being  introduced  for  municipal  water treatment,  for  example
           the European Union Urban Waste Water Treatment Directive (UWWTD) and the
           position taken by the UK Drinking Water Inspectorate regarding cryptosporidia,
           portend continued growth in this sector for membrane technology. Indeed, the
           EU  wastewater  treatment  membrane  market  is  predicted  to  increase  by  an
           average annual growth rate of  5.9% to $2 50 million in 2006 (RCC, 2002).
             Application  of  membrane  processes  within  the  industrial  sector  is  also
           widespread  and  well  established  in  many  instances.  Reverse  osmosis  and
           ultrafiltration, for  example, are both widely  used  within the pharmaceutical
           industry to remove pyrogens in the provision of water for injection (WFI). These
           processes  are  also  essential  in  providing  ultrapure  water  in  semiconductor
           fabrication plant, where ultrafiltration  is used  for removing  colloidal material
           and reverse osmosis both for primary deionisation (followed by polishing using
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