Title of article :
Particulate-biofilm, expanded-bed technology for high-rate, low-cost wastewater treatment: Nitrification
Author/Authors :
M.J. Dempsey، نويسنده , , K.C. Lannigan، نويسنده , , R.J. Minall، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2005
Pages :
10
From page :
965
To page :
974
Abstract :
The performance of a particulate-biofilm, expanded-bed process for nitrification of activated sludge final effluent (ASFE) is reported for a plant receiving mixed industrial and domestic wastewater. The support material for the particulate-biofilms was glassy coke, to which the nitrifying bacteria attached and formed a highly active biofilm. An average nitrification rate of 1.7±0.6 kg m−3expanded bed d−1 was recorded during operation of the bioreactor, which had a hydraulic residence time of 15 min. On average, the ASFE contained 12.6±3.7 g m−3 NH3–N, which was reduced to 2.6±3.3 g m−3 NH3–N. Furthermore, transfer of 10–12% of the oxygen in air was achieved using counter-current aeration. This investigation has demonstrated that a high rate of nitrification can be achieved with a particulate-biofilm, expanded-bed process. It has also demonstrated that the process can operate without backwashing and still remove particulate material from the ASFE feed.
Keywords :
wastewater treatment , Ammonia oxidation , Nitrification , Expanded bed , Particulate biofilm , Fluidised bed
Journal title :
Water Research
Serial Year :
2005
Journal title :
Water Research
Record number :
772317
Link To Document :
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