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Denitrification in Tertiary Filtration: Application of an Up-Flow Filter

机译:三次过滤中的反硝化:上流式过滤器的应用

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The present paper shows the results obtained through an experimental work performed at the wastewater treatment plant of Rome, aimed at studying the performances of a tertiary filter regarding combined removal of suspended solids, COD, and nitrates. The up-flow sand filter was fed by the effluent coming from the secondary settling tank of the plant. The filter bed height was of 80 cm of silica sand. After a start up period, a study of particulate and soluble COD removal process was made, to establish the need of methanol in the deni-trification process. Total COD removal efficiency was 60% on average, 55% due by soluble COD removal and 5% by particulate one. In the last phase of the experimental activity methanol was fed as carbon source, sodium sulfite was supplied to produce anoxic environment within the filter and the denitrification efficiency was studied. Nitrates removal rates after an acclimation period of 10 days increased up to 60%, with an effluent NO_3-N of 8mg/L. Denitrification rate was 2.4 kg/m~3 d for water temperatures of 25℃. Regarding methanol demand and biologic kinetics, the biomass yield coefficient was 0.3 kg_(COD-X)-x/kg_(me). Consequently 2.7 kg of methanol was required per required per kilogram of denitrified nitrogen.
机译:本文显示了通过在罗马的废水处理厂进行的实验工作获得的结果,旨在研究有关联合去除悬浮固体,COD和硝酸盐的第三级过滤器的性能。上流式砂滤池由工厂二级沉淀池的废水进料。滤床高度为80厘米的硅砂。在启动阶段之后,对颗粒和可溶性COD去除过程进行了研究,以确定在反硝化过程中需要甲醇。总的COD去除效率平均为60%,其中可溶性COD去除率为55%,微粒去除率为5%。在实验活动的最后阶段,以甲醇作为碳源,提供亚硫酸钠以在过滤器内产生缺氧环境,并研究了脱氮效率。适应10天后的硝酸盐去除率提高到60%,出水NO_3-N为8mg / L。在25℃的水温下,反硝化速率为2.4kg / m〜3 d。关于甲醇需求和生物动力学,生物质产率系数为0.3kg_(COD-X)-x / kg_(me)。因此,每公斤反硝化氮气每需要2.7公斤甲醇。

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