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生物脱氮工艺设计中的几个问题 被引量:4

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摘要 生物脱氮系统工艺设计的主要内容包括确定硝化池和反硝化池容积、供气量、碱需要量、回流比和碳源需要量等。本文作者介绍了常见的硝化池和反硝化池容积、硝化反应需氧量及碱需要量的计算方法,并对常见的硝化池和反硝化池容积的计算方法进行了讨论。
作者 章非娟
机构地区 同济大学
出处 《给水排水》 CSCD 北大核心 1997年第4期21-24,共4页 Water & Wastewater Engineering
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  • 1金仁村,郑平,陈建伟,屠展.三相逆流湍动床气液传质性能的研究[J].生物工程学报,2007,23(1):122-126. 被引量:7
  • 2唐建国.德国一段硝化和反硝化活性污泥法曝气池的设计计算(下)[J].给水排水,1997,23(2):57-60. 被引量:1
  • 3Van der Star W R L, Abma W R, Bolmmers D, et al. Startup of reactors for anoxic ammonium oxidation: Experiences from the first full-scale anammox reactor in Rotterdam [ J ]. Water Research, 2007, 41: 4149-4163.
  • 4Tsushima I, Ogasawara Y, Kindaichi T, et al. Development of high-rate anaerobic ammonium-oxidizing (anammox) biofilm reactors[J]. Water Research, 2007, 41(8) : 1623-1634.
  • 5Ruiz G, Jeison D, Chamy R. Nitrification with high nitrite accumulation for the treatment of wastewater with high ammonia concentration [ J ]. Water Research, 37 ( 6 ) : 1371 - 1377.
  • 6Buffiere P, Bergeon J P, Moletta R. The inverse turbulent bed: a novel biureactor for anaerobic treatment [ J ]. Water Research, 2000, 34(2) : 673-677.
  • 7Bernet N, Sanchez O, Dabert P, et al. Effect of solid hold-up on nitrite accumulation in a biofilm reactor-molecular characterization of nitrifying communities [ J]. Water Science and Technology, 2004,49(11/12) : 123-130.
  • 8Bougard D, Bernet N, Cheneby D, et al. Nitrification of a high- strength wastewater in an inverse turbulent bed reactor: Effect of temperature on nitrite accumulation [ J ]. Process Biochemistry, 2006, 41(1) : 106-113.
  • 9Bernet N, Sanchez O, Cesbron D, et al. Modeling and control of nitrite accumulation in a nitrifying biofilm reactor [ J ]. Biochemical Engineering Journal, 2005, 24(2) : 173-183.
  • 10Arnaiz C, Gutierrez J C, Lebrato J. Support material selection for anaerobic fluidized bed reactors by phospholipid analysis [ J ]. Biochemical Engineering Journal, 2006, 32 : 240-245.

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