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Particulate-biofilm, expanded-bed technology for high-rate, low-cost wastewater treatment: Nitrification

机译:用于高速率,低成本废水处理的颗粒生物膜膨胀床技术:硝化作用

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摘要

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.
机译:据报道,某工厂接受工业和生活污水的混合处理时,采用了颗粒生物膜膨胀床硝化活性污泥最终废水(ASFE)的性能。颗粒生物膜的支撑材料是玻璃状焦炭,硝化作用是细菌附着并形成高活性生物膜。在生物反应器运行期间记录的平均硝化速率为1.7±0.6 kg m-3膨胀床d-1,其水力停留时间为15分钟。平均而言,ASFE含有12.6±3.7 g m-3 NH3-N,减少到2.6±3.3 g m-3 NH3-N。此外,使用逆流曝气可实现空气中10–12%的氧气转移。这项研究表明,采用颗粒生物膜膨胀床工艺可以实现较高的硝化率。还证明了该方法无需反洗即可运行,并且仍可从ASFE进料中去除颗粒物质。

著录项

  • 作者

    Dempsey Michael J.;

  • 作者单位
  • 年度 2006
  • 总页数
  • 原文格式 PDF
  • 正文语种 {"code":"en","name":"English","id":9}
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