首页> 外文期刊>Journal of Environmental Science and Health. A, Toxic/Hazardous Substances & Environmental Engineering >Novel Phased Isolation Ditch System for Enhanced Nutrient Removal and Its Optimal Operating Strategy
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Novel Phased Isolation Ditch System for Enhanced Nutrient Removal and Its Optimal Operating Strategy

机译:新型相控隔离沟渠系统,用于强化养分去除及其最佳运行策略

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Phased isolation ditch system with intrachannel clarifier is a simplified novel oxidation ditch system enhancing simultaneous removal of biological nitrogen and phosphorus in municipal wastewater. The system employs two ditches with intra-clarifier, and eliminates external final clarifier, additional preanaerobic reactor, and recycle of sludge and nitrified effluent. Separation of anoxic, anaerobic, and aerobic phases can be accomplished by alternating flow and intermittent aeration. Its pilot-scale system operated at HRTs of 10-21 h, SRTs of 15-41 days, and a cycle times of 2-8 h showed removals of BOD, TN, and TP in the range of mixed liquor temperature above 10℃ as high as 88-97, 70-84, and 65-90%, respectively. As the SRTs became longer, the effluent TN decreased dramatically, whereas the effluent TP increased. Higher nitrogen removal was accomplished at shorter cycle times, while better phosphorus removal was achieved in longer cycle times. Optimal system operating strategies maximizing the performance and satisfying both the best nitrogen and phosphorus removals included HRTs ranged 10-14h, SRTs ranged 25-30 days, and a cycle time of 4h at the mixed liquor temperature above 10℃. Thus, complete phase separation in a cycle maximizing phosphorus release and uptake as well as nitrification and denitrification was accomplished by scheduling of alternating flow and intermittent aeration in the simplified process scheme. Especially, temporal phase separation for phosphorus release without additional anaerobic reactor was successfully accomplished during anaerobic period without any nitrate interference and carbon-limiting.
机译:带通道内澄清池的相控隔离沟系统是简化的新型氧化沟系统,可同时去除市政废水中的生物氮和磷。该系统采用带有内部澄清池的两个沟渠,并消除了外部最终澄清池,额外的厌氧反应器以及污泥和硝化废水的再循环。缺氧,厌氧和好氧相的分离可以通过交替流动和间歇通气来实现。其中试规模的系统在HRT为10-21h,SRT为15-41天,周期为2-8h的情况下显示,在10℃以上的混合液温度范围内,去除了BOD,TN和TP。分别高达88-97%,70-84和65-90%。随着SRT的延长,出水TN急剧下降,而出水TP增加。在较短的循环时间内可以实现更高的脱氮率,而在较长的循环时间内可以实现更好的脱磷。使性能最大化并满足最佳氮和磷去除率的最佳系统操作策略包括:HRT范围为10-14h,SRT范围为25-30天,在混合液温度高于10℃时循环时间为4h。因此,在简化的工艺方案中,通过安排交替流动和间歇通气,可以最大程度地实现磷释放和吸收以及硝化和反硝化的最大循环。尤其是,在没有任何硝酸盐干扰和碳限制的情况下,在厌氧期间成功完成了无需附加厌氧反应器的磷释放的时间相分离。

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