[PDF][PDF] Feasibility of utilizing moving bed biofilm reactor to upgrade and retrofit municipal wastewater treatment plants
AH Javid, AH Hassani, B Ghanbari… - International Journal of …, 2013 - ijer.ut.ac.ir
In this study, feasibility of upgrading and retrofitting municipal wastewater treatment
plantswas investigated at laboratory scale using Moving Bed Biofilm Reactor (MBBR)
process. For this purpose, an aerobic pilot was operated for nearly one year in different
conditions, in which a moving bed carrier with aspecific biofilm surface area of 500 m2/m3
and a filling rate of 60% was utilized. System efficiency in removal of BOD5 and COD was
examined at different hydraulic retention times (HRTs) of 1, 1.5, 2, 2.5, 3 and 4 h. The …
plantswas investigated at laboratory scale using Moving Bed Biofilm Reactor (MBBR)
process. For this purpose, an aerobic pilot was operated for nearly one year in different
conditions, in which a moving bed carrier with aspecific biofilm surface area of 500 m2/m3
and a filling rate of 60% was utilized. System efficiency in removal of BOD5 and COD was
examined at different hydraulic retention times (HRTs) of 1, 1.5, 2, 2.5, 3 and 4 h. The …
Feasibility of utilizing moving bed biofilm reactor to upgrade and retrofit municipal wastewater treatment plants
J AH, H AH - 2013 - pesquisa.bvsalud.org
In this study, feasibility of upgrading and retrofitting municipal wastewater treatment plants
was investigated at laboratory scale using Moving Bed Biofilm Reactor [MBBR] process. For
this purpose, an aerobic pilot was operated for nearly one year in different conditions, in
which a moving bed carrier with a specific biofilm surface area of 500 m [2]/m [3] and a filling
rate of 60% was utilized. System efficiency in removal of BOD [5] and COD was examined at
different hydraulic retention times [HRTs] of 1, 1.5, 2, 2.5, 3 and 4 h. The obtained results …
was investigated at laboratory scale using Moving Bed Biofilm Reactor [MBBR] process. For
this purpose, an aerobic pilot was operated for nearly one year in different conditions, in
which a moving bed carrier with a specific biofilm surface area of 500 m [2]/m [3] and a filling
rate of 60% was utilized. System efficiency in removal of BOD [5] and COD was examined at
different hydraulic retention times [HRTs] of 1, 1.5, 2, 2.5, 3 and 4 h. The obtained results …
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