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dc.contributor.authorSnowdon Joshua;Singh Kripa S.;Zanatta Gustavo
dc.date.accessioned2019-02-26T07:56:52Z
dc.date.available2019-02-26T07:56:52Z
dc.date.issued2018
dc.identifier.other%28ASCE%29EE.1943-7870.0001376.pdf
dc.identifier.urihttp://yetl.yabesh.ir/yetl1/handle/yetl/4250460
dc.description.abstractMembrane and reactor performance for an anaerobic membrane bioreactor (AnMBR) treating a high-strength starch-based wastewater [average chemical oxygen demand (COD) of 84.8±8.9  g/L] was examined under six varied cleaning protocols to find optimal operating conditions. The AnMBR was composed of a 1,-L anaerobic continuous stirred tank reactor (CSTR) integrated with an external, tubular nanofiltration membrane module operated in cross-flow mode. The polyvinylidene fluoride–based membrane module had a nominal pore size of 3 nm, a total membrane area of .42  m2, and a cross-flow velocity of 2.5  m/s. The different cleaning protocols were provided by varying the membrane’s permeate backwash duration, frequency, and flow rate and by incorporating chemically enhanced backwash cycles with the use of a mixed 25-ppm sodium hydroxide and 25-ppm hypochlorite solution. Reactor performance did not appear to be cleaning protocol dependent; however, a decline in reactor-specific methanogenic activity (SMA) was noticed over the duration of the study. A single, longer-duration chemically enhanced backwash offered the highest improvement in membrane performance over all other cleaning protocols.
dc.publisherAmerican Society of Civil Engineers
dc.titleOptimization of an External Nanofiltration Anaerobic Membrane Bioreactor Treating a High-Strength Starch-Based Wastewater
dc.typeJournal Paper
dc.journal.volume144
dc.journal.issue6
dc.journal.titleJournal of Environmental Engineering
dc.identifier.doi10.1061/(ASCE)EE.1943-7870.0001376
dc.page4018032
dc.treeJournal of Environmental Engineering:;2018:;Volume ( 144 ):;issue: 006
dc.contenttypeFulltext


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