2012
DOI: 10.1080/19443994.2012.708538
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Bio-entrapped membrane reactor for organic matter removal and membrane fouling reduction

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Cited by 8 publications
(3 citation statements)
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“…In addition, the period between membrane cleanings was prolonged from 60 to 140 days [227]. Ng et al [228] developed the bio-entrapped membrane reactor (BEMR) packed with bio-ball carriers and operated nearly 4 times longer than conventional MBR before reaching critical TMP, thus, contributing to reduced chemical cleaning frequency [229]. Rafiei et al [224] demonstrated that a bio-entrapped MBR with cells entrapped in polyurethane foam provided better results with regard to membrane fouling and removal efficiencies of COD, ammonium and phenol, when compared to biofilm and conventional MBRs.…”
Section: 4mentioning
confidence: 99%
“…In addition, the period between membrane cleanings was prolonged from 60 to 140 days [227]. Ng et al [228] developed the bio-entrapped membrane reactor (BEMR) packed with bio-ball carriers and operated nearly 4 times longer than conventional MBR before reaching critical TMP, thus, contributing to reduced chemical cleaning frequency [229]. Rafiei et al [224] demonstrated that a bio-entrapped MBR with cells entrapped in polyurethane foam provided better results with regard to membrane fouling and removal efficiencies of COD, ammonium and phenol, when compared to biofilm and conventional MBRs.…”
Section: 4mentioning
confidence: 99%
“…The NH þ 4 -N concentration profile is very similar to the COD profile as NH þ 4 -N is nitrified in the presence of DO; it follows that nitrifying bacteria are distributed only near the surface of the EMMC ball where DO is available. In the presence of DO and substrates, the EMMC carriers have good contact with them at the outer region, where nitrification process is very active [12]. Our previous experimental results showed that the pH stayed constant around 7.1-7.4 at the influent side and 6.6-6.9 at the effluent side.…”
Section: Resultsmentioning
confidence: 84%
“…Therefore, the mass transfer resistance of solutes is greater at the boundary layer that limits the overall mass transfer. Wang et al [10] and Yu et al [11] studied simultaneous carbon and nitrogen removal from wastewater of different compositions, and Ng et al [12] operated bio-entrapped membrane operation in different modes to treat wastewater of the food and beverage industry. The biochemical processes occurred at the inter macrospores between the carrier balls and the intra microspores within the carrier.…”
Section: Conceptual Modelmentioning
confidence: 99%