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Modeling nitrogen removal with partial nitritation and anammox in one floc-based sequencing batch reactor

机译:在一个基于絮团的顺序分批反应器中通过部分硝化和厌氧氨氮模拟脱氮

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摘要

Full-scale application of partial nitritation and anammox in a single floc-based sequencing batch reactor (SBR) has been achieved for high-rate nitrogen (N) removal, but mechanisms resulting in reliable operation are not well understood. In this work, a mathematical model was calibrated and validated to evaluate operating conditions that lead to out-competition of nitrite oxidizers (NOB) from the SBRs and allow to maintain high anammox activity during long-term operation. The validity of the model was tested using experimental data from two independent previously reported floc-based full-scale SBRs for N-removal via partial nitritation and anammox, with different aeration strategies at aeration phase (continuous vs. intermittent aeration). The model described the SBR cycle profiles and long-term dynamic data from the two SBR plants sufficiently and provided insights into the dynamics of microbial population fractions and N-removal performance. Ammonium oxidation and anammox reaction could occur simultaneously at DO range of 0.15 -0.3 mg O_2 L~(-1) at aeration phase under continuous aeration condition, allowing simplified process control compared to intermittent aeration. The oxygen supply beyond prompt depletion by ammonium oxidizers (AOB) would lead to the growth of NOB competing with anammox for nitrite. NOB could also be washed out of the system and high anammox fractions could be maintained by controlling sludge age higher than 40 days and DO at around 0.2 mg O_2 L~(-1). Furthermore, the results suggest that N-removal in SBR occurs via both alternating nitritation/anammox and simultaneous nitritation/anammox, supporting an alternative strategy to improve N-removal in this promising treatment process, i.e., different anaerobic phases can be implemented in the SBR-cycle configuration.
机译:已经实现了在单个基于絮凝的顺序分批反应器(SBR)中实现部分硝化和厌氧氨氮的大规模应用,以实现高速率的氮(N)去除,但是导致可靠运行的机理尚未得到很好的理解。在这项工作中,已对数学模型进行了校准和验证,以评估导致SBR超越亚硝酸氧化剂(NOB)的竞争条件,并在长期运行过程中保持较高的厌氧氨氧化活性。使用来自两个独立的先前报道的基于絮凝的全尺寸SBR通过部分硝化和厌氧氨氮脱氮的实验数据测试了模型的有效性,在曝气阶段采用了不同的曝气策略(连续曝气与间歇曝气)。该模型充分描述了两个SBR工厂的SBR循环曲线和长期动态数据,并提供了有关微生物种群组成和N去除性能动态的见解。在连续曝气条件下,在曝气阶段,DO浓度为0.15 -0.3 mg O_2 L〜(-1)时,氨氧化和厌氧氨氧化反应可同时发生,与间歇曝气相比,简化了过程控制。氨气氧化剂(AOB)迅速消耗掉的氧气将导致NOB与厌氧氨水竞争亚硝酸盐的增长。还可以将NOB洗出系统,并通过控制污泥龄超过40天和DO保持在约0.2 mg O_2 L〜(-1)来维持较高的厌氧菌含量。此外,结果表明,SBR中的氮去除通过交替硝化/厌氧和同时硝化/厌氧氨发生,支持了在这一有前途的处理过程中改善氮去除的替代策略,即可以在SBR中实施不同的厌氧相。 -周期配置。

著录项

  • 来源
    《Water Research》 |2014年第15期|321-329|共9页
  • 作者单位

    Advanced Water Management Centre, The University of Queensland, St. Lucia, Queensland 4072, Australia;

    Advanced Water Management Centre, The University of Queensland, St. Lucia, Queensland 4072, Australia,Eawag, Swiss Federal Institute of Aquatic Science and Technology, Ueberlandstr. 133, 8600 Duebendorf, Switzerland;

    Advanced Water Management Centre, The University of Queensland, St. Lucia, Queensland 4072, Australia;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Nitrogen removal; Anammox; Dissolved oxygen; Nitritation; Nitrite oxidizers; Sequencing batch reactor;

    机译:脱氮;Anammox;溶解氧;亚硝化亚硝酸盐氧化剂;顺序批处理反应器;

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