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Complete nitrogen removal from municipal wastewater via partial nitrification by appropriately alternating anoxic/aerobic conditions in a continuous plug-flow step feed process

机译:在连续推流步骤进料过程中,通过适当交替的缺氧/好氧条件,通过部分硝化作用,从市政废水中完全去除氮

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摘要

This study assessed the technical feasibility of removing nitrogen from municipal waste-water by partial nitrification (nitritation) in a continuous plug-flow step feed process. Nitrite in the effluent accumulated to over 81.5 ± 9.2% but disappeared with the transition of process operation from anoxic/oxic mode to the anaerobic/anoxic/oxic mode. Batch tests showed obvious ammonia oxidizing bacteria (AOB) stimulation (advanced ammonia oxidation rate) and nitrite (NOB) oxidizing bacteria inhibition (reduced nitrite oxidation rate) under transient anoxic conditions. Two main factors contributed to nitritation in this continuous plug-flow process: One was the alternating anoxic and oxic operational condition; the step feed strategy guaranteed timely denitrification in anoxic zones, allowing a reduction in energy supply (nitrite) to NOB. Fluorescence in Situ Hybridization and quantitative real-time polymerase chain reaction analysis indicated that NOB population gradually decreased to 1.0 ± 0.1% of the total bacterial population (dominant Nitrospira spp., 1.55 × 10~9 copies/L) while AOB increased approximately two-fold (7.4 ± 0.9%, 1.25 × 10~(10) copies/L) during the above anoxic to anaerobic transition. Most importantly, without addition of external carbon sources, the above wastewater treatment process reached 86.0 ± 4.2% of total nitrogen (TN) removal with only 7.23 ± 2.31 mg/L of TN in the effluent, which met the discharge requirements.
机译:这项研究评估了在连续推流式进料过程中通过部分硝化(硝化)从市政废水中去除氮的技术可行性。废水中的亚硝酸盐累积超过81.5±9.2%,但随着过程操作从缺氧/有氧模式转换为厌氧/缺氧/有氧模式而消失。批处理测试显示,在短暂缺氧条件下,明显的氨氧化细菌(AOB)刺激(高级氨氧化速率)和亚硝酸盐(NOB)氧化细菌抑制作用(亚硝酸盐氧化速率降低)。在这种连续的塞流过程中,导致硝化作用的主要因素有两个:一是交替的缺氧和有氧操作条件;二是交替运行。分步进料策略可确保在缺氧区域及时进行反硝化,从而减少NOB的能源供应(亚硝酸盐)。荧光原位杂交和定量实时聚合酶链反应分析表明,NOB群体逐渐减少至总细菌群体的1.0±0.1%(主要的硝化螺菌属菌种,为1.55×10〜9拷贝/ L),而AOB则增加了约2-在上述从缺氧到厌氧的过渡过程中,其折叠倍数为(7.4±0.9%,1.25×10〜(10)拷贝/ L)。最重要的是,在不添加外部碳源的情况下,上述废水处理过程达到了总氮(TN)去除量的86.0±4.2%,而废水中的TN仅达到7.23±2.31 mg / L,满足了排放要求。

著录项

  • 来源
    《Water Research》 |2014年第15期|95-105|共11页
  • 作者单位

    Key Laboratory of Beijing Water Quality Science and Water Environment Recovery Engineering, Engineering Research Center of Beijing, Beijing University of Technology, Beijing 100124, PR China;

    Key Laboratory of Beijing Water Quality Science and Water Environment Recovery Engineering, Engineering Research Center of Beijing, Beijing University of Technology, Beijing 100124, PR China;

    College of Graduate Studies, State University of New York Upstate Medical University, Syracuse, NY 13210, USA;

    Key Laboratory of Beijing Water Quality Science and Water Environment Recovery Engineering, Engineering Research Center of Beijing, Beijing University of Technology, Beijing 100124, PR China;

    State Key Laboratory of Urban Water Resource and Environment, Harbin Institute of Technology, Harbin 150090, PR China;

  • 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

    Partial nitrification; Nitritation; Biological nutrient removal; Wastewater; Step feed;

    机译:部分硝化;亚硝化生物营养去除废水;分步进给;
  • 入库时间 2022-08-17 13:44:25

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