• Title/Summary/Keyword: airlift biofilm reactor

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Biofilm airlift 반응기를 이용한 선택적 질산화의 연구

  • Yun, Ho-Jun;Jang, Jae-Seon;Kim, Dong-Jin
    • 한국생물공학회:학술대회논문집
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    • 2000.11a
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    • pp.457-460
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    • 2000
  • A biofilm airlift reactor filled with biomass-covered carriers (sand) were used to remove ammonium by selective nitrification (ammonium to nitrite). The effects of experimental conditions (ammonium load, pH, dissolved oxygen) on nitrification and nitrite accumulation were investigated. The reactor showed more than 90% nitrification efficiencies at 2.5 kg $NH_4\;^+-N/m^3/d$ and $NO_2\;^--N$ could be accumulated between 75% and 90% in the effluent. It is likely that nitratation (nitrite oxidizer) was inhibited by low dissolved oxygen concentration while nitritation (ammonium oxidizer) was kept stable.

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A Study on the Distribution of Nitrite Oxidation Microorganisms in a Biofilm Reactor

  • Yoon, Joung-Yee;Kim, Sun-Hee;Kim, Dong-Jin
    • 한국생물공학회:학술대회논문집
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    • 2005.04a
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    • pp.282-286
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    • 2005
  • Biofilm airlift reactor was continuously operated to investigate the competitions between the autotrophs and heterotrophs, ammonia oxidizers and nitrite oxidizers, and Nitrobacter and Nitrospira with real wastewater at a C/N ratio of 0.86. As the reactor achieved complete nitrification microbial distribution was analyzed by FISH/CLSM technique. The results showed that heterotroph was more abundant than nitrifying bacteria. Ammonia oxidizers (17%) and Nitrobacter (7%) prevailed nitrite oxidizers (9%) and Nitrospira (2%), respectively.

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The Simultaneous Nitrification and Organics Oxidation of Wastewater in Airlift Biofilm Reactors (공기리프트 생물막 반응기에서의 폐수 질화 및 유기물 동시산화)

  • 서일순;허충희
    • KSBB Journal
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    • v.16 no.6
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    • pp.573-578
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    • 2001
  • The effects of organic supplement (acetate) and dissolved oxygen concentration on the nitrification rate of wastewater were investigated in the 27.7 L pilot-scale airlift biofilm reactor with the granular activated carbon media of 0.613 mm diameter. The ammonium oxidation rate increased stepwise up to 5 kg N/㎥$.$d at the riser air velocity of 0.063 m/s, when the air velocity and the ammonium loading rate were raised alternately. The nitrite build-up was observed during the early stage of the biofilm formation, which disappeared after the reactor operation of 128 days. As increasing the organic loading rate, the organic oxidation rate increased up to 25.0 kg COD/㎥$.$d with the removal efficiency of 94% but the oxidation rates of ammonium and nitrite decreased. The oxidation rates of ammonium and nitrite increased with the dissolved oxygen concentrations. When the pure oxygen was sparged, the ammonium oxidation rate was almost five times higher than that with air at the same velocity.

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