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采用液体循环的序批式生物膜反应器进行硝化/反硝化处理后处理的可行性。

Feasibility of nitrification/denitrification in a sequencing batch biofilm reactor with liquid circulation applied to post-treatment.

作者信息

Andrade do Canto Catarina Simone, Rodrigues José Alberto Domingues, Ratusznei Suzana Maria, Zaiat Marcelo, Foresti Eugênio

机构信息

Escola de Engenharia Mauá, Instituto Mauá de Tecnologia, Praça Mauá, 1, CEP 09580-900, São Caetano do Sul, SP, Brazil.

出版信息

Bioresour Technol. 2008 Feb;99(3):644-54. doi: 10.1016/j.biortech.2006.12.040. Epub 2007 Mar 2.

Abstract

An investigation was performed on the biological removal of ammonium nitrogen from synthetic wastewater by the simultaneous nitrification/denitrification (SND) process, using a sequencing batch biofilm reactor (SBBR). System behavior was analyzed as to the effects of sludge type used as inoculum (autotrophic/heterotrophic), wastewater feed strategy (batch/fed-batch) and aeration strategy (continuous/intermittent). The presence of an autotrophic aerobic sludge showed to be essential for nitrification startup, despite publications stating the existence of heterotrophic organisms capable of nitrifying organic and inorganic nitrogen compounds at low dissolved oxygen concentrations. As to feed strategy, batch operation (synthetic wastewater containing 100 mg COD/L and 50 mg N-NH(4)(+)/L) followed by fed-batch (synthetic wastewater with 100 mg COD/L) during a whole cycle seemed to be the most adequate, mainly during the denitrification phase. Regarding aeration strategy, an intermittent mode, with dissolved oxygen concentration of 2.0mg/L in the aeration phase, showed the best results. Under these optimal conditions, 97% of influent ammonium nitrogen (80% of total nitrogen) was removed at a rate of 86.5 mg N-NH(4)(+)/Ld. In the treated effluent only 0.2 mg N-NO(2)(-)/L,4.6 mg N-NO(3)(-)/L and 1.0 mg N-NH(4)(+)/L remained, demonstrating the potential viability of this process in post-treatment of wastewaters containing ammonium nitrogen.

摘要

利用序批式生物膜反应器(SBBR),通过同步硝化/反硝化(SND)工艺对合成废水中的氨氮生物去除进行了研究。分析了系统行为,涉及用作接种物的污泥类型(自养/异养)、废水进料策略(分批/补料分批)和曝气策略(连续/间歇)的影响。尽管有文献表明存在能够在低溶解氧浓度下硝化有机和无机氮化合物的异养生物,但自养好氧污泥的存在对硝化启动至关重要。至于进料策略,在整个周期中先进行分批操作(含有100mg COD/L和50mg N-NH₄⁺/L的合成废水),然后进行补料分批操作(含有100mg COD/L的合成废水)似乎是最合适的,主要是在反硝化阶段。关于曝气策略,曝气阶段溶解氧浓度为2.0mg/L的间歇模式显示出最佳效果。在这些最佳条件下,以86.5mg N-NH₄⁺/L·d的速率去除了97%的进水氨氮(占总氮的80%)。在处理后的流出物中,仅残留0.2mg N-NO₂⁻/L、4.6mg N-NO₃⁻/L和1.0mg N-NH₄⁺/L,证明了该工艺在含氨氮废水后处理中的潜在可行性。

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