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Model-based control structure design of a full-scale WWTP under the retrofitting process

机译:改造过程中大型污水处理厂基于模型的控制结构设计

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The anoxic-oxic (A/O) municipal wastewater treatment plant (WWTP) of Manresa (Catalonia, Spain) was studied for a possible conversion to an anaerobic/anoxic/oxic (A(2)/O) configuration to promote enhanced biological phosphorus removal. The control structure had to be redesigned to satisfy the new necessity to control phosphorus concentration, besides ammonium and nitrate concentrations (main pollutant concentrations). Thereby, decentralized control structures with proportional-integralderivative (PID) controllers and centralized control structures with model-predictive controllers (MPC) were designed and tested. All the designed control structures had their performance systematically tested regarding effluent quality and operating costs. The centralized control structure, A(2)/O-3-MPC, achieved the lowest operating costs with the best effluent quality using the A(2)/O plant configuration for the Manresa WWTP. The controlled variables used in this control structure were ammonium in the effluent, nitrate at the end of the anoxic zone and phosphate at the end of the anaerobic zone, while the manipulated variables were the internal and external recycle flow rates and the dissolved oxygen setpoint in the aerobic reactors.
机译:研究了曼雷萨(西班牙加泰罗尼亚)的缺氧(A / O)市政废水处理厂(WWTP)可能转换为厌氧/缺氧/有氧(A(2)/ O)配置以促进增强的生物磷去除。必须重新设计控制结构,以满足除铵和硝酸盐浓度(主要污染物浓度)之外控制磷浓度的新需要。因此,设计并测试了具有比例积分微分(PID)控制器的分散控制结构和具有模型预测控制器(MPC)的集中控制结构。所有设计的控制结构都针对废水质量和运营成本进行了系统性能测试。集中式控制结构A(2)/ O-3-MPC使用Manresa污水处理厂的A(2)/ O工厂配置实现了最低的运营成本和最佳的废水质量。在此控制结构中使用的控制变量是废水中的铵,缺氧区域末端的硝酸盐和厌氧区域末端的磷酸盐,而受控变量是内部和外部循环流量以及溶解氧设定值。好氧反应堆。

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