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硝化活性污泥工艺中的最优曝气控制。

Optimal aeration control in a nitrifying activated sludge process.

机构信息

IVL Swedish Environmental Research Institute, P.O. Box 210 60, 100 31 Stockholm, Sweden.

出版信息

Water Res. 2012 May 1;46(7):2101-10. doi: 10.1016/j.watres.2012.01.023. Epub 2012 Jan 28.

Abstract

An important tool to minimise energy consumption in activated sludge processes is to control the aeration system. Aeration is a costly process and the dissolved oxygen level will determine the efficiency of the operation as well as the treatment results. What aeration control should achieve is closely linked to how the effluent criteria are defined. This paper explores how the aeration process should be controlled to meet the effluent discharge limits in an energy efficient manner in countries where the effluent nitrogen criterion is defined as average values over long time frames, such as months or years. Simulations have been performed using a simplified Benchmark Simulation Model No. 1 to investigate the effect of different levels of suppressing the variations of the effluent ammonium concentration. Optimisation is performed where the manipulated variable for aeration (the oxygen transfer coefficient, K(L)a) is minimised with the constraint that the average daily flow-proportional ammonium concentration in the effluent should reach a desired level. The optimisation results are compared with constant dissolved oxygen concentrations and supervisory ammonium control with different controller settings. The results demonstrate and explain how and why energy consumption can be optimised by tolerating the ammonium concentration to vary around a given average value. In these simulations, the optimal oxygen peak-to-peak amplitude range between 0.7 and 1.8 mg/l depending on the influent variation and ammonium level in the effluent. These variations can be achieved with a slow ammonium feedback controller. The air flow requirements can be reduced by 1-4% compared to constant dissolved oxygen set-points. Optimal control of aeration requires up to 14% less energy than needed for fast feedback control of effluent ammonium.

摘要

一种减少活性污泥工艺中能耗的重要工具是控制曝气系统。曝气是一个成本高昂的过程,溶解氧水平将决定操作效率和处理结果。曝气控制应该达到的目标与如何定义出水标准密切相关。本文探讨了在以国家为单位的层面上,如何以节能的方式控制曝气过程,以满足排放限制,这些国家的出水氮标准是在很长一段时间内(如几个月或几年)的平均值定义的。使用简化的基准模拟模型 1 进行了模拟,以研究不同程度抑制出水氨氮浓度变化的效果。优化是在曝气(氧传递系数 K(L)a)的操纵变量最小的情况下进行的,其约束条件是出水中与每日流量成比例的氨氮浓度应达到期望水平。将优化结果与恒定溶解氧浓度和具有不同控制器设置的监督性氨氮控制进行了比较。结果表明并解释了为什么以及为什么可以通过容忍氨氮浓度围绕给定平均值变化来优化能耗。在这些模拟中,最优氧峰峰值幅度范围在 0.7 至 1.8 mg/l 之间,具体取决于进水变化和出水氨氮水平。这些变化可以通过缓慢的氨氮反馈控制器来实现。与恒定溶解氧设定点相比,空气流量要求可降低 1-4%。曝气的最优控制所需的能量比需要快速反馈控制出水氨氮所需的能量少 14%。

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