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Sustainable nitrogen removal by denitrifying anammox applied for anaerobic pre-treated potato wastewater

机译:厌氧预处理马铃薯废水中反硝化厌氧氨氮的可持续去除

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The feasibility of sustainable nitrogen removal was investigated in a two stage biofilm configuration consisting of a MBBR (Moving Bed Biofilm Reactor) and a Deamox reactor (Biobed-EGSB). The MBBR is used for nitrification and the denitrifying ammonium oxidation (Deamox) is aimed at a nitrogen removal process in which part of the required nitrite for the typical anammox reaction originated from nitrate. Anaerobic pre-treated potato wastewater was supplied to a MBBR and Deamox reactor operated in series with a bypass flow of 30%. The MBBR showed stable nitrite production at ammonium-loading rates of 0.9-1.0 kg NH_4-N/m~3 d with ammonium conversion rates of 0.80-0.85 kg NH_4-N/m~3 d. The nitrogen-loading rate and conversion rate of the Deamox reactor were 1.6-1.8 and 1.6 kg N/m~3 d. The maximum ammonium removal capacity in the Deamox reactor was 0.6 kg NH4-N/m3 d. The removal efficiency of soluble total nitrogen reached 90%. The Deamox process performance was found to be negatively affected during decline of the operating temperature from 33 to 22 °C and by organic loading rates with a chemical oxygen demand (COD)/NO_2-N ratio >1.
机译:在包括MBBR(移动床生物膜反应器)和Deamox反应器(Biobed-EGSB)的两阶段生物膜配置中研究了可持续脱氮的可行性。 MBBR用于硝化,反硝化氨氧化(Deamox)的目标是脱氮过程,在该过程中,典型厌氧氨氧化反应所需的部分亚硝酸盐源自硝酸盐。厌氧预处理的马铃薯废水被供应到MBBR和Deamox反应器中,该反应器以30%的旁路流量串联运行。 MBBR在铵负载量为0.9-1.0 kg NH_4-N / m〜3 d时显示稳定的亚硝酸盐生成,铵转化率为0.80〜0.85 kg NH_4-N / m〜3 d。脱氨反应器的氮气负载率和转化率分别为1.6-1.8和1.6 kg N / m〜3 d。 Deamox反应器中的最大铵去除量为0.6 kg NH4-N / m3 d。可溶性总氮的去除率达到90%。发现在工作温度从33降低到22°C期间,以及有机物加载速率(化学需氧量(COD)/ NO_2-N之比> 1)对Deamox工艺性能的负面影响。

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