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Membrane technology  67

           Table 2.15  Common foulants and their pretreatment, reverse osmosis

           Foulant             Effect on performance    Pretreatment
                                                    ~
           Suspended solids    Decrease in permeability,   < 2 mg IF1:  5 pm cartridge filter;
                               normally in first stage   > 2 mg I-':  multimedia deep-bed
                                                        filter
                                                        Cross-flow microfiltration
           Organic and inorganic   As above             Ultrafiltration
           colloidal matter,                            Precoat filtration
           SDI  5                                       Multimedia deep bed filtration
                                                        In-line coagulation and filtration
                                                        Softening
           Alkaline scales: CaC03   Decrease in salt rejection and   LSI  < 2: threshold inhibitor dosing:
                               slight decrease in permeability,   LSI > 2: acid addition: LSI n 2: ion
                               normally in ha1 stage    exchange or lime-soda softening
           Active silica       As above                 Lime-soda softening with MgO
                                                        Alkali dosing
                                                        Heat
           Permanent hardness   As above                Scale inhibitor dosing, ion
                                                        exchange softening, lime-soda
                                                        softening
           Sulphate scales, e.g.   As above             Threshold inhibitors
           CaS04
           Metal oxide (iron and   As above             Aeration and filtration, dissolved
           manganese)                                   air flotation (DAF), catalytic
                                                        oxidation (greensand filtration),
                                                        chemical oxidation and filtration
           Free chlorine       Permanent loss of rejection due   Activated carbon, chemical
                               to degradation ofmembrane"   reducing agent
           Dissolved organics. e.g.   Rapid decrease in permeability   Adsorption (GAC), flotation
           NOM, EPS, anionic
           detergents
           Biological matter   Decrease in permeability   Chlorination/dechlorination.
                                                        UV (+ microfiltration)
           a Non-chlorine-resistant  materials.


           permeate  water  in  the  reverse  direction  through  the  membrane,  and  the
           cleaning  cycle in which  the membrane is invariably  chemically treated  for a
           more extended period. Whilst both backflushing and cleaning are routinely and
           advantageously  employed to recover some of  the flux, nonetheless incur a cost
           penalty through:

             a  the energy consumption,
             a  the loss of product water,
             a  the downtime, and
             a  the use of hazardous chemicals.

             The energy consumption  relates to the hydraulic resistance, as discussed in
           Section  2.4.2. The  loss  of  product  water  arises  because  of  its  use  for  both
           backflushing and cleaning, and can be significant. For example, a 20 s backflush
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