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Electrochemical disinfection and removal of ammonia nitrogen for the reclamation of wastewater treatment plant effluent

机译:氨氮去除氨氮的电化学消毒及去除废水处理厂流出物

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Residual ammonia and pathogenic microorganisms restrict the reclamation and reuse of wastewater treatment plant (WWTP) effluent. An electrochemical system was developed for the simultaneous removal of ammonia and disinfection of actual WWTP effluent. The performance of the electrochemical process on synthetic wastewater at different chloride ion concentrations was also investigated. Results demonstrated that the optimal chloride concentration for ammonia and Escherichia coli (E. coli) removal was 250 mg/L. Successful disinfection of E. coli in actual effluent was achieved at 0.072 Ah/L, but the inverse S-type inactivation curve indicated that there was a competitive consumption of strong oxidants and chloramines working as another disinfectant. A higher electric charge (0.58 Ah/L) was required to simultaneously reduce E. coli and ammonia to levels that meet the reclamation requirements for WWTP effluent. At this electric charge, no trihalomethane, chlorate, or perchlorate in the system was observed, indicating the biological safety of this process. These results demonstrate the potential of this electrochemical process as a tertiary wastewater treatment process for WWTP effluent reclamation purposes.
机译:残留的氨和病原微生物限制废水处理厂(WWTP)流出物的回收和再利用。开发了一种电化学系统,用于同时去除氨和实际WWTP流出物的消毒。还研究了在不同氯离子浓度下对合成废水的电化学方法的性能。结果表明,氨和大肠杆菌(大肠杆菌)去除的最佳氯化物浓度为250mg / L.在实际流出物中成功消毒在实际流出物中以0.072 AH / L实现,但逆S型失活曲线表明,竞争消耗强烈的氧化剂和作为另一个消毒剂的氯胺。需要更高的电荷(0.58Ah / L),以同时降低大肠杆菌和氨,以满足WWTP流出物的填海病因的水平。在该电荷下,观察到系统中没有三卤甲烷,氯酸盐或高氯酸盐,表明该方法的生物安全性。这些结果证明了这种电化学过程作为拟氢废水处理过程的巨型废水处理方法。

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