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首页> 外文期刊>Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies >Feasibility of nitrification/denitrification in a sequencing batch biofilm reactor with liquid circulation applied to post-treatment
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Feasibility of nitrification/denitrification in a sequencing batch biofilm reactor with liquid circulation applied to post-treatment

机译:在测序间歇式生物膜反应器中进行液体循环进行硝化/反硝化的可行性

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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-NH4+/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 2.0 mg/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-NH4+/L d. In the treated effluent only 0.2 mg N-NO2-/L, 4.6 mg N-NO3/L and 1.0 mg N-NH4+/L remained, demonstrating the potential viability of this process in post-treatment of wastewaters containing ammonium nitrogen. (c) 2007 Elsevier Ltd. All rights reserved.
机译:通过使用同步批处理生物膜反应器(SBBR),通过同时硝化/反硝化(SND)工艺从合成废水中生物去除铵氮进行了研究。分析了系统行为,包括污泥类型(接种物)(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。尽管有出版物指出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,但自养需氧污泥的存在对硝化启动至关重要。对于进料策略,在整个周期内分批操作(含100 mg COD / L和50 mg N-NH4 + / L的合成废水),然后分批进料(含100 mg 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,在曝气阶段采用溶解氧浓度为2.0 mg / L的间歇模式显示了最佳效果。在这些最佳条件下,以86.5 mg N-NH4 + / L d的速率去除了97%的流入铵态氮(占总氮的80%)。在经过处理的废水中,仅残留0.2 mg N-NO2- / L,4.6 mg N-NO3 / L和1.0 mg N-NH4 + / L,证明了该方法在含铵氮废水的后处理中的潜在可行性。 (c)2007 Elsevier Ltd.保留所有权利。

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