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contributor authorA. di Biase
contributor authorT. R. Devlin
contributor authorJ. A. Oleszkiewicz
date accessioned2017-12-16T09:16:49Z
date available2017-12-16T09:16:49Z
date issued2016
identifier other%28ASCE%29EE.1943-7870.0001146.pdf
identifier urihttp://138.201.223.254:8080/yetl1/handle/yetl/4240897
description abstractTwo 4-L anaerobic moving bed–biofilm reactors (AMBBR) with different quantities of cubic media (25 and 35% by volume) were examined. Reactors were fed synthetic protein-based feed and both were shown to be capable of treating up to 20  kg/m3 day of chemical oxygen demand (COD), achieving 80% COD removal. Beyond that load the performance began to decrease. The maximum biogas production observed was 9.25  m3 CH4/m3  day at an organic loading rate (OLR) of 20  kg COD/m3 day. The methane composition varied between 60 and 70%. Averaged methane yields of 0.36±0.07  m3 CH4/kg COD removed and specific removal rates from 0.4 to 20  kg COD/m3 day were achieved. At the maximum OLR above 20  kg COD/m3 day, the specific surface area activity was calculated as 98 and 75  g COD/m2 day in the 25 and 35% reactors, respectively. Kinetic tests performed at the maximum OLR revealed that free-floating suspended biomass contributed to no more than 2.5% of the total removal. The reactors were also capable of treating brewery wastewater, reliably attaining 80% COD removal with methane yields of 0.36±0.06 and 0.39±0.03  m3 CH4/kg COD from the 35 and 25% reactors, respectively.
publisherAmerican Society of Civil Engineers
titleStart-Up of an Anaerobic Moving Bed–Biofilm Reactor and Transition to Brewery Wastewater Treatment
typeJournal Paper
journal volume142
journal issue12
journal titleJournal of Environmental Engineering
identifier doi10.1061/(ASCE)EE.1943-7870.0001146
treeJournal of Environmental Engineering:;2016:;Volume ( 142 ):;issue: 012
contenttypeFulltext


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