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    Start-Up of an Anaerobic Moving Bed–Biofilm Reactor and Transition to Brewery Wastewater Treatment

    Source: Journal of Environmental Engineering:;2016:;Volume ( 142 ):;issue: 012
    Author:
    A. di Biase
    ,
    T. R. Devlin
    ,
    J. A. Oleszkiewicz
    DOI: 10.1061/(ASCE)EE.1943-7870.0001146
    Publisher: American Society of Civil Engineers
    Abstract: Two 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.
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      Start-Up of an Anaerobic Moving Bed–Biofilm Reactor and Transition to Brewery Wastewater Treatment

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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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