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OPTIMISED OPERATION AND DESIGN OF ALTERNATING ACTIVATED SLUDGE PROCESSES FOR NREMOVAL

机译:脱氮交替活性污泥工艺的优化操作和设计

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This paper presents a simulation study with the scope to optimise the plant design and oper- ation strategy of 2-reactors alternating activated sludge processes with only flow. schedule and aeration on/off as control inputs. The methodology is to simulate the application of receding horizon optimal control (RHOC) to a range of different plant designs within this class of systems and select the combi- nation of design and operation strategy with the best performance. Subsequently a simple feedback con- troller is designed that closely imitates the optimal operation strategy. Starting-point is the plant layout with maximal degree of freedom within the above-mentioned class (Fig. l ), which is commercially avail- able under the name BIODENITROD. The simulation results indicate that in the optimal combination of plant design and operation strategy the performance in terms of nitrogen removal improves signifi- cantly as compared to current practice, especially if a shorter cycle length is used. In the optimal pro- cess design the two reactors are placed in series, the first reactor is about four times as large as the second one. The possibilities of feeding influent to reactor 2 and withdrauwing effluent from reactor 1 are redundant. A conceptually simple feedback controller (OSCAR, operating a series connection of two alternating reactors) is presented that straightforwardly implements the improved operation strategy.
机译:本文提出了一个模拟研究,其范围旨在优化仅具有流量的两反应器交替活性污泥工艺的工厂设计和运行策略。安排和充气开/关作为控制输入。该方法论是模拟后退水平最优控制(RHOC)在此类系统中对一系列不同工厂设计的应用,并选择性能最佳的设计和运营策略的组合。随后,设计了一个简单的反馈控制器,它紧密地模仿了最佳的操作策略。起点是在上述类别(图1)中具有最大自由度的工厂布局,可以以BIODENITROD的名称在市场上买到。仿真结果表明,与目前的实践相比,在工厂设计和运营策略的最佳组合下,除氮性能显着提高,尤其是在使用较短的循环长度的情况下。在最佳过程设计中,两个反应器串联放置,第一个反应器的尺寸约为第二个反应器的四倍。将流体进料到反应器2和排出来自反应器1的流出物是多余的。提出了一种概念上简单的反馈控制器(OSCAR,操作两个交替电抗器的串联连接),可以直接实现改进的操作策略。

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