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Nitrification with high nitrite accumulation for the treatment of wastewater with high ammonia concentration

机译:高亚硝酸盐积累的硝化处理高氨氮废水。

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The objective of this paper was to determine the best conditions for partial nitrification with nitrite accumulation of simulated industrial wastewater with high ammonia concentration, lowering the total oxygen needed in the nitrification step, which may mean great saving in aeration. Dissolved oxygen (DO) concentration and pH were selected as operational parameters to study the possibility of nitrite accumulation not affecting overall ammonia removal. A 2.5 L activated sludge reactor was operated in nitrification mode, feeding a synthetic wastewater simulating an industrial wastewater with high ammonia concentration. During the start-up a pH of 7.85 and a DO of 5.5 mg/L were used. The reactor was operated until stable operation was achieved at final nitrogen loading rate (NLR) of 3.3 kg N- NH_4~+/m~3 d with an influent ammonia concentration of 610mg N-NH_4~+/L. The influence of pH was studied in continuous operation in the range of 6.15-9.05, changing the reactor pH in steps until ammonia accumulation (complete nitrification inhibition) took place. The influence of DO was studied in the same mode, changing the DO in steps from 5.5 to 0.5mg/L. The pH was not a useful operational parameter in order to accumulate nitrite, because in the range of pH 6.45-8.95 complete nitrification to nitrate occurs. At pH lower than 6.45 and higher than 8.95 complete inhibition of nitrification takes place. Setting DO concentration in the reactor at 0.7mg/L, it was possible to accumulate more than 65% of the loaded ammonia nitrogen as nitrite with a 98% ammonia conversion. Below 0.5mg/L of DO ammonia was accumulated and over a DO of 1.7mg/L complete nitrification to nitrate was achieved. In conclusion, it is possible under the conditions of this study, to treat high ammonia synthetic wastewater achieving an accumulation of at least 65% of the loaded nitrogen as nitrite, operating at a DO around 0.7mg/L. This represents a reduction close to 20% in the oxygen necessary, and therefore a considerable saving in aeration.
机译:本文的目的是确定模拟高氨浓度工业废水中亚硝酸盐积累的部分硝化的最佳条件,从而降低硝化步骤所需的总氧气,这可能意味着节省大量的曝气。选择溶解氧(DO)浓度和pH作为操作参数,以研究亚硝酸盐积累不会影响整体氨气去除的可能性。 2.5 L活性污泥反应器在硝化模式下运行,向合成废水中添加模拟高氨浓度的工业废水。在启动过程中,使用的pH值为7.85,溶解度为5.5 mg / L。使反应器运行直至在3.3kg N-NH_4〜+ / m〜3 d的最终氮负载率(NLR)和进水氨浓度为610mg N-NH_4〜+ / L的情况下达到稳定运行为止。在连续操作范围为6.15-9.05的范围内研究了pH的影响,逐步改变反应器的pH值直到氨气积累(完全硝化抑制)为止。在相同的模式下研究溶解氧的影响,将溶解氧从5.5mg / L逐步改变为0.5mg / L。 pH值不是用于累积亚硝酸盐的有用操作参数,因为在pH 6.45-8.95的范围内会发生完全硝化为硝酸盐的情况。在pH值低于6.45和高于8.95时,完全抑制了硝化作用。将反应器中的DO浓度设置为0.7mg / L,可以以98%的氨转化率收集超过65%的亚硝酸盐负载氨氮。低于0.5mg / L的DO积累了氨,超过1.7mg / L的DO则完全硝化为硝酸盐。总之,在本研究的条件下,可以处理高氨合成废水,该废水的亚硝酸盐含量至少达到氮含量的65%,在DO约为0.7mg / L的条件下运行。这表示所需的氧气减少了近20%,因此大大节省了充气。

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