Please use this identifier to cite or link to this item: https://dspace.ctu.edu.vn/jspui/handle/123456789/71715
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dc.contributor.authorNguyen, P.T.-
dc.contributor.authorDang, B.T.-
dc.contributor.authorPham, H.D.-
dc.contributor.authorHuynh, Q.T.-
dc.contributor.authorNguyen, X.D.-
dc.contributor.authorNguyen, H.H.-
dc.contributor.authorLee, K.J.-
dc.contributor.authorBui, X.T.-
dc.date.accessioned2021-12-30T08:21:28Z-
dc.date.available2021-12-30T08:21:28Z-
dc.date.issued2020-
dc.identifier.issn2525-2461-
dc.identifier.urihttps://dspace.ctu.edu.vn/jspui/handle/123456789/71715-
dc.description.abstractMembrane bioreactors (MBRs) are being increasingly applied to many full-scale plants around the world to treat both municipal and industrial wastewater. However, membrane fouling and energy consumption are significant challenges to broader applications of MBRs. By using a new MBR configuration, this research aims to compare the performance between a conventional MBR and a reciprocation MBR (rMBR) that uses inertial forces without air scouring for fouling reduction. The results show that there was no difference in chemical oxygen demand (COD) (92-98%) or total nitrogen (TN) (71-77%) after 280 d of operation under the same influent constraints. However, by using the inertial force, the fouling rates were 0.35 mbar/d for the rMBR, resulting in a significantly lower fouling rate in comparison with a conventional MBR and other literature reports. Thus, the lower energy consumption over long-term operation of a rMBR could be a promising solution to overcome the drawbacks of a MBR.vi_VN
dc.language.isoenvi_VN
dc.relation.ispartofseriesVietnam Journal of Science, Technology and Engineering;Vol. 62, No. 01 .- P.50-54-
dc.subjectEnergy consumptionvi_VN
dc.subjectFoulingvi_VN
dc.subjectReciprocation membrane bioreactorvi_VN
dc.titleEvaluating the membrane fouling control ability of a reciprocation membrane bioreactor (rMBR) systemvi_VN
dc.typeArticlevi_VN
Appears in Collections:Vietnam journal of Science, Technology and Engineering

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