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Ammonium removal from primary and secondary effluents using a bioregenerated ion-exchange process

机译:使用生物再生离子交换工艺从一级和二级废水中去除铵

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A new process for ammonia removal from sewage effluents is presented. The process uses an ion exchange material, zeolite, both as the separator of NH_4~+ from the wastewater and also as the carrier for a nitrifying biomass. The process is carried out in a single reactor operating in two modes: an adsorption mode in which the zeolite column acts as a typical ion exchanger and a bioregeneration mode in which the bacteria attached to the zeolite oxidizes the NH_4~+ to NO_3~-. The separation between carbonaceous removal and NH_4~+ removal enables the exclusive selection of nitrifiers at high concentrations attached to the zeolite, thus achieving high bioregeneration rates. This paper summarizes three years of research on the process and focuses on the operation with actual secondary and primary effluents. Process operation showed: (1) no bed clogging occurred due to suspended solids accumulation; (2) residual BOD from the adsorption phase resulted in only minimal heterotroph competition and thus, no fall in the rate of bioregeneration; (3) only a small deterioration in exchange efficiency due to zeolite biofilm coverage as compared to the ion exchange efficiency of "virgin" zeolite. Results show that both secondary and primary effluents can be successfully treated by the process.
机译:提出了一种从污水中去除氨的新方法。该方法使用离子交换材料沸石,既作为废水中NH_4 +的分离剂,又作为硝化生物质的载体。该方法在单一反应器中以两种模式运行:在吸附模式下,沸石柱用作典型的离子交换剂;在生物再生模式下,附着在沸石上的细菌将NH_4〜+氧化为NO_3〜-。碳质去除和NH_4 ++去除之间的分离使得能够独家选择附着在沸石上的高浓度硝化器,从而实现高生物再生率。本文总结了对该过程的三年研究,并着重于实际二级和一级废水的操作。工艺操作表明:(1)没有因悬浮物堆积而造成床层堵塞; (2)吸附相中残留的BOD仅导致最小的异养菌竞争,因此生物再生速率没有下降; (3)与“原始”沸石的离子交换效率相比,由于沸石生物膜的覆盖而导致的交换效率仅小幅下降。结果表明,该工艺可以成功处理次要废水和主要废水。

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