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Combining submerged membrane technology with anaerobic and ...

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Impact of a methanogenic pre-treatment on the performance of an aerobic MBR systemreuse both in agriculture <strong>and</strong> as heating or cooling water or for cleaning purposes,depending on the quality st<strong>and</strong>ards.The methanogenic treatment could affect results obtained in aerobic MBRs. Partialdegradation products coming from the treatment of complex substrates in themethanogenic stage might have a negative impact on <strong>membrane</strong> performance. Wilén et al.(2000) observed that a complex substrate as activated sludge flocs deflocculated under<strong>anaerobic</strong> conditions. The deflocculated particles were mainly bacteria <strong>and</strong> floc fragments,although some soluble polymeric substances were also released. Therefore, the hydrolysisof complex substrates such as aerobic sludge (for instance coming from the recirculationbetween aerobic <strong>and</strong> methanogenic stages) could lead to a release of biopolymers,affecting <strong>membrane</strong> fouling.The fraction of biopolymers most frequently mentioned in relation <strong>with</strong> <strong>membrane</strong>fouling is the group of soluble microbial products (SMP). This group contains soluble <strong>and</strong>colloidal biopolymers, mostly carbohydrates (SMPc) <strong>and</strong> proteins (SMPp) (Drews, 2010).SMPc has been widely considered as the most important parameter regarding <strong>membrane</strong>fouling (Rosenberger et al., 2006; Drews, 2010). Nevertheless, recent studies haveintroduced a more general approach to the biopolymers responsible for <strong>membrane</strong> foulingby defining biopolymer cluster (BPC) <strong>and</strong> transparent exopolymer particles (TEP) asimportant factors in the formation of the sludge fouling layer on the <strong>membrane</strong> surface <strong>and</strong>the increase of fouling potential (Sun et al., 2008; de la Torre et al., 2008). BPC have beendefined as a pool of non-filterable organic matter in the liquid phase of the MBR sludgemixture much larger than SMP (Sun et al., 2008) whereas TEP are very sticky particlesthat exhibit the characteristics of gels, <strong>and</strong> consist predominantly of acidic polysaccharides(Passow, 2002). Depending on the applied assays, these groups are not distinct butoverlap (Drews, 2010).Different post-treatment systems for UASB effluents have been widely studied,among them aerobic MBRs being one of the most recent <strong>and</strong> not yet understoodpossibilities (Chong et al., 2012). Therefore, it is of prime importance to identify <strong>and</strong>underst<strong>and</strong> the causes responsible for <strong>membrane</strong> fouling in these systems.5.2. ObjectivesThe objective of this work was to study <strong>membrane</strong> fouling in an aerobic MBR after amethanogenic pre-treatment of low-strength wastewater at ambient temperatures.131

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