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Combining submerged membrane technology with anaerobic and ...

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Introductionutilizes the advantages of a biofilm reactor <strong>and</strong> which at the same time can h<strong>and</strong>le highloads of particles.The Moving Bed Bioreactor (MBBR) consists in an activated-sludge system wherethe biomass is attached to the carriers suspended in the mixed liquor. These carriers havea great internal surface in order to improve the optimal contact of liquid, oxygen <strong>and</strong>biomass. It is in the internal surface where the development of the biofilm takes place. This<strong>technology</strong> addresses some of the most important challenges of the Water <strong>and</strong>Wastewater industry, such as the upgrading of existing treatment plants <strong>and</strong> tight nutrientdischarge limits (Frost & Sullivan, 2009).From the combination of this <strong>technology</strong> <strong>with</strong> the <strong>technology</strong> of <strong>membrane</strong>bioreactors is born today a new system called Biofilm Membrane Bioreactor (BF-MBR)also called moving bed <strong>membrane</strong> bioreactor (MBMBR) (Leikness <strong>and</strong> Ødegaard, 2007)(figure 1.9). This system would present an alternative to the activated sludge MBR bycombining a biofilm reactor <strong>with</strong> <strong>membrane</strong> separation of the suspended solids (BF-MBR),which may reduce the effect of <strong>membrane</strong> fouling by high biomass concentrations. The<strong>membrane</strong> module in this kind of systems is located in a separate chamber from thatcontaining the carriers in order to avoid possible damages in the <strong>membrane</strong>.MOVING BEDBIOFILM REACTORMEMBRANEREACTORpermeateinfluentSludgeairFigure 1.9. Biofilm Membrane Bioreactor (Leikness <strong>and</strong> Ødegaard, 2007).BF-MBR process has the potential of operating <strong>with</strong> volumetric loading rates of 2-8kg COD·m -3·d-1 , higher than those observed in typical MBRs of 1-3 kg COD·m -3·d-1 , <strong>and</strong>HRTs up to 4 h. Sustainable process operation <strong>with</strong> <strong>membrane</strong> fluxes around 50 L·m-2·h-1can be achieved in BF-MBR (Leikness <strong>and</strong> Ødegaard, 2007), which are much higher than49

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