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Cost-performance analysis of nutrient removal in a full-scale oxidation ditch process based on kinetic modeling

机译:基于动力学模型的全规模氧化沟工艺养分去除的成本效益分析

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摘要

A full-scale oxidation ditch process for treating sewage was simulated with the ASM2d model and optimized for minimal cost with acceptable performance in terms of ammonium and phosphorus removal. A unified index was introduced by integrating operational costs (aeration energy and sludge production) with effluent violations for performance evaluation. Scenario analysis showed that, in comparison with the baseline (all of the 9 aerators activated), the strategy of activating 5 aerators could save aeration energy significantly with an ammonium violation below 10%. Sludge discharge scenario analysis showed that a sludge discharge flow of 250-300 m~3/day (solid retention time (SRT), 13-15 days) was appropriate for the enhancement of phosphorus removal without excessive sludge production. The proposed optimal control strategy was: activating 5 rotating disks operated with a mode of "111100100" ("1" represents activation and "0" represents inactivation) for aeration and sludge discharge flow of 200 m~3/day (SRT, 19 days). Compared with the baseline, this strategy could achieve ammonium violation below 10% and TP violation below 30% with substantial reduction of aeration energy cost (46%) and minimal increment of sludge production (< 2%). This study provides a useful approach for the optimization of process operation and control.
机译:使用ASM2d模型模拟了用于污水处理的全规模氧化沟工艺,并针对最小的成本进行了优化,并且在去除铵和磷方面表现出令人满意的性能。通过将运营成本(曝气能量和污泥生产)与废水违法行为相结合来引入统一指标,以进行绩效评估。情景分析表明,与基线(所有9个曝气机均已激活)相比,激活5个曝气机的策略可在氨气违规率低于10%的情况下显着节省曝气能量。污泥排放情景分析表明,250-300 m〜3 /天的污泥排放流量(固体保留时间(SRT),13-15天)适合于在不产生过多污泥的情况下提高除磷效率。提议的最佳控制策略是:激活5个以“ 111100100”模式运行的转盘(“ 1”表示激活,“ 0”表示灭活),曝气和污泥排出流量为200 m〜3 / day(SRT,19天) )。与基准线相比,该策略可以实现氨气违规率低于10%,总磷违规率低于30%,同时大幅降低曝气能源成本(46%),并使污泥产生的增量最小(<2%)。这项研究为优化过程操作和控制提供了有用的方法。

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