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Benchmarking combined biological phosphorus and nitrogen removal wastewater treatment processes

机译:基准联合生物除磷和脱氮废水处理工艺

摘要

This paper describes the implementation of a simulation benchmark for studying the influence of control strategy implementations on combined nitrogen and phosphorus removal processes in a biological wastewater treatment plant. The presented simulation benchmark plant and its performance criteria are to a large extent based on the already existing nitrogen removal simulation benchmark. The paper illustrates and motivates the selection of the treatment plant lay-out, the selection of the biological process model, the development of realistic influent disturbance scenarios for dry, rain and storm weather conditions respectively, the definition of performance indexes that include the phosphorus removal processes, and the selection of a suitable operating point for the plant. Two control loops were implemented: one for dissolved oxygen control using the oxygen transfer coefficient KLa as manipulated variable, the second one for nitrate control in the anoxic zone using the internal recirculation flow rate as manipulated variable. Dynamic simulations for different dissolved oxygen set points illustrate the complex interactions in this plant, and the necessity for a continuous trade off between supplying sufficient oxygen to promote nitrification on the one hand, and the need for low dissolved oxygen concentrations on the other hand to allow sufficient development of phosphorus accumulating organisms. The potential for aeration energy savings in the plant is highlighted based on the dissolved oxygen profiles resulting from open loop simulations with a dynamic dry weather influent scenario. The influence of the dissolved oxygen set point selection on the nitrate control loop performance observed in the simulations further illustrates the need for a plant-wide optimization approach to reach optimal plant performance.
机译:本文介绍了模拟基准的实现,该基准用于研究控制策略实施对生物废水处理厂中氮和磷联合去除过程的影响。所提出的模拟基准工厂及其性能标准在很大程度上基于现有的脱氮模拟基准。本文说明并激励了处理厂布局的选择,生物过程模型的选择,分别针对干旱,雨水和暴风雨天气条件的实际进水扰动情景的发展以及包括除磷在内的性能指标的定义过程,以及为工厂选择合适的工作点。实施了两个控制回路:一个用于使用氧传递系数KLa作为调节变量的溶解氧控制,第二个用于使用内部再循环流速作为调节变量的缺氧区域中的硝酸盐控制。不同溶解氧设定点的动态模拟说明了该工厂中的复杂相互作用,一方面需要在提供足够的氧气以促进硝化作用之间进行持续权衡,另一方面需要低溶解氧浓度以允许磷积累生物的充分发展。根据开环模拟和动态干旱天气情况下产生的溶解氧曲线,强调了工厂中通气节能的潜力。在模拟中观察到的溶解氧设定点选择对硝酸盐控制回路性能的影响进一步表明,需要一种全厂范围的优化方法来达到最佳的工厂性能。

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