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Research on effect of simultaneous nitrification denitrification under step-feed with three-stage catching bed reactor

机译:三级捕集床反应器分步进料同时硝化反硝化效果研究

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Three-stage catching bed reactor was used to treat domestic wastewater from residential area through the step feed in order to get high efficiency of simultaneous nitrification denitrification(SND). The effect of 3 influent flow rate distribution ratios (λ) on the removal of COD, NH4+-N and TN was investigated under the conditions of hydraulic retention time (HRT)=8h, DO=1.0∼2.0mg/L and sludge reflux rate of 100%. The removal efficiency of TN and NH4+-N reached at 70.9%, 96.4% separately when λ was 3∶4∶3; When λ was controlled in 4∶3∶3∶62.7% of average TN removal rate was obtained and the removal efficiency of NH4+-N was 95.8%; When λ was adjusted to 5∶3∶2, the removal efficiency of TN decreased to 58.5%. However, nitrification is still very good, 90.6% of average NH4+-N removal rate was achieved. And more than 90% of average COD removal rate was obtained under the three projects of flow rate distribution.
机译:为了实现同步硝化反硝化(SND)的高效率,使用三级捕集床反应器通过分步进料处理居民区的生活污水。在水力停留时间(HRT)条件下,研究了3种进水流量分配比(λ)对COD,NH 4 + -N和TN的去除效果)= 8h,DO = 1.0〜2.0mg / L,污泥回流率为100%。当λ为3∶4∶3时,TN和NH 4 + -N的去除效率分别达到70.9%和96.4%。当将λ控制在TN的平均去除率为4∶3∶3∶62.7%时,NH 4 + -N的去除率为95.8%;当λ调整为5∶3∶2时,TN的去除率降至58.5%。然而,硝化作用仍然很好,达到了平均NH 4 + -N去除率的90.6%。在三个流量分布计划下,平均COD去除率达到90%以上。

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