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Combining submerged membrane technology with anaerobic and ...

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IntroductionSubmerged MBR system in municipal applications, represent the 99% of the installed<strong>membrane</strong> surface in Europe in the period 2002–05. On the other h<strong>and</strong>, side-streamconfiguration is commonly used in industrial applications. In general, <strong>submerged</strong> MBRrequire higher initial investment costs, <strong>and</strong> aeration <strong>with</strong> respect to side-stream <strong>membrane</strong>configurations. In contrast, pumping costs are lower <strong>and</strong> operating, requiring loweroperating flows <strong>and</strong> cleaning frequencies (Stephenson et al., 2000). The selection between<strong>submerged</strong> <strong>and</strong> side-stream configurations for aerobic MBRs seems somehow settled, infavour of <strong>submerged</strong> MBRs. In fact, nowadays, most of the commercial applications arebased on the <strong>submerged</strong> configuration, due to lower associated energy requirements(Judd, 2011).Today there are approaching 60 MBR <strong>membrane</strong> module products available <strong>and</strong> thenumber of <strong>technology</strong> suppliers continues to exp<strong>and</strong>. On table 1.2 can be observed themanufacturers of <strong>submerged</strong> <strong>membrane</strong> <strong>technology</strong>, both flat sheet <strong>and</strong> hollow fiber.1.4. Tertiary <strong>membrane</strong> filtrationTertiary filtration, especially depth filtration, has been traditionally used to removesuspended solids from secondary treated waters. They can also be used to removeparticulate <strong>and</strong> colloidal matter from settled secondary effluents, which increases theeffectiveness of disinfection <strong>with</strong> either ultraviolet radiation or ozone for reuse applications(Tchobanoglous et al., 1998; Lubello et al., 2003). However, in recent years, the use oftertiary <strong>membrane</strong> filtration systems is becoming more common.For tertiary filtration applications, MF <strong>and</strong> UF <strong>membrane</strong> systems can be divided intwo different types: <strong>submerged</strong>, when the <strong>membrane</strong>s are <strong>submerged</strong> in a feed water tankwhere permeate is sucked (via vacuum) into the inside of the <strong>membrane</strong> (dead-endfiltration); <strong>and</strong> pressurized (or contained), when the <strong>membrane</strong>s are housed in moduleswhere pressurized feed water is forced through the fiber <strong>and</strong> permeate is collect on theoutside (cross-filtration). In turn, FS or HF <strong>membrane</strong>s can be used in <strong>submerged</strong> systemswhereas contained systems are composed by HF or MT ones (Li et al. 2008). Submerged<strong>membrane</strong> modules have gained popularity, especially for low solids feeds, because of thelower costs associated <strong>and</strong> the acceptance of modest fluxes <strong>and</strong> low trans<strong>membrane</strong>pressures (TMP).Low-pressure tertiary <strong>membrane</strong>s have been proved to meet increasingly stringentst<strong>and</strong>ards for discharge or reuse. In fact, more than 78% of wastewater reclamation plantsused low-pressure <strong>membrane</strong>s as a pretreatment for the reverse osmosis process39

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