2010
DOI: 10.1016/j.desal.2008.11.042
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Filterability in a submerged anaerobic membrane bioreactor

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Cited by 54 publications
(26 citation statements)
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“…The maximum flux of AnFB-MBR achieved was higher than those between 5 and 10 L m −2 h −1 observed in anaerobic membrane bioreactors (Ho and Sung 2010;Spagni et al 2010) but lower than those typically reported in aerobic MBRs, being between 20 and 25 L m −2 h −1 (Judd 2002). Anaerobic membrane bioreactors have potential for energy-efficient treatment of wastewater treatment, membrane fouling being a major hurdle to application (Kim et al 2011).…”
Section: Discussionmentioning
confidence: 96%
“…The maximum flux of AnFB-MBR achieved was higher than those between 5 and 10 L m −2 h −1 observed in anaerobic membrane bioreactors (Ho and Sung 2010;Spagni et al 2010) but lower than those typically reported in aerobic MBRs, being between 20 and 25 L m −2 h −1 (Judd 2002). Anaerobic membrane bioreactors have potential for energy-efficient treatment of wastewater treatment, membrane fouling being a major hurdle to application (Kim et al 2011).…”
Section: Discussionmentioning
confidence: 96%
“…After this, due to a high increase in TMP, [7] sludge was extracted to control the total suspended solids (TSS) and TMP. Thereafter, the solids retention time (SRT) was controlled at approximately 50 d.…”
Section: Methodsmentioning
confidence: 99%
“…[9] The aim of this study was to evaluate the applicability of the ADM1 to a submerged AMBR (SAMBR) treating simulated industrial wastewater and applying a wide range of organic loading rates. This study follows two previous studies in which sludge filterability [7] and reactor performances [28] were described in detail.…”
Section: Introductionmentioning
confidence: 99%
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“…On the other hand, submerged membrane bioreactors are less energy intense, but require larger membrane surface area to ensure high permeate fluxes, easy cleaning in comparison to their external loop counterparts (Bakonyi et al, 2014). The internal looped SAMBR has many advantage over UASBr and ASPs, viz: a) achieving high quality permeate retaining maximum suspended solids that can convert particulate COD (COD P ) to soluble COD (COD S ) for enriched biogas production and eliminating the need for secondary clarifier, b) operating the reactors with an increased level of biomass (12-20 g.L À1 ) (Spagni et al, 2009), c) high substrate to biomass (Food to microorganism) ratio in the reactor (Mahendran et al, 2011), d) efficient gas, liquid and solids (GLS) separation (Bakonyi et al, 2014) and f) high substrate to bacterial contact without any sludge gradient through mixing of SAMBR by self-synthesized and stored biogas (Smith et al, 2013;Lin et al, 2010;Jeison and Lier, 2006) as a biogas mixing and dispersion/agitation arrangements. Consequently, many researchers have demonstrated SAMBR as an efficient treatment for low and high strength sewage and industrial wastewaters Gao et al, 2011;Xu et al, 2011;Lindmark et al, 2011;Zayen et al, 2010;Saddoud et al, 2007).…”
Section: Introductionmentioning
confidence: 99%