• 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