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Process control design and analysis for wastewater disinfection, stream neutralization, and run-to-run strategies.

机译:用于废水消毒,水流中和和逐项运行策略的过程控制设计和分析。

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The wastewater chlorination process in fixed-size open-channel reactors is a challenging control problem because of the presence of a variable dead time caused by changes in the inlet flow rate. The approach proposed here involves the utilization of a moving weir as an actuator in a novel residence time control scheme, designed to ensure that fluid passing through the reactor experiences a constant residence time independent of flow rate. The dynamic weir control loop is conceived to supplement existing control structures that are charged with manipulating the dosage of chlorine. Simulations studies show that both feedforward and feedback manifestations of the residence time controller are highly effective at improving chlorine dosage control and are highly robust with respect to weir-flow modeling and measurement errors. In fact, these controllers have the potential to improve the control performance dramatically while saving as much as 45% of the chlorine used for treatment.; An automatic control system described as run-to-run is one in which a discrete controller is applied to an inherently discrete process, and where the performance measurements are made only after all processing is completed. A complete theoretical analysis is developed for the case of a static plant under proportional-integral control, resulting in quantitative descriptions of the nominal and robust stability regions, and recommended tuning heuristics. The analysis for the case of a Smith Predictor design shows that very small modeling errors in the estimated measurement delay may cause closed-loop instability. Therefore, the use of a Smith Predictor for run-to-run systems suffering from uncertainty in the delay is not recommended.; A weak-acid/strong-base neutralization control system utilizing two alternative pH sensors is modeled and analyzed. The first sensor is a traditional pH electrode whose output signal is proportional to pH, and the second sensor is a fiber-optic optrode that produces a signal that is proportional to hydrogen ion concentration. Systematic simulation studies show that no inherent performance improvement is observed when using the optrode instead of the electrode sensor in the feedback loop.
机译:固定尺寸明渠反应器中的废水氯化过程是一个具有挑战性的控制问题,因为存在因进水流速变化而导致的可变死区时间的存在。本文提出的方法涉及在新颖的停留时间控制方案中利用活动堰作为致动器,该停留时间控制方案旨在确保流经反应器的流体经历与流量无关的恒定停留时间。动态堰控制回路被构想为补充现有的控制结构,该控制结构负责操纵氯的剂量。仿真研究表明,滞留时间控制器的前馈和反馈形式在改善氯剂量控制方面非常有效,并且在堰流模型和测量误差方面也非常可靠。实际上,这些控制器有潜力显着改善控制性能,同时节省多达45%的处理氯。一种称为“运行到运行”的自动控制系统,其中将离散控制器应用于固有的离散过程,并且仅在所有处理完成后才进行性能测量。针对在比例积分控制下的静态工厂的情况,开发了完整的理论分析,从而对标称和鲁棒稳定性区域进行了定量描述,并推荐了调整启发法。对Smith Smith预测器设计情况的分析表明,估计的测量延迟中很小的建模误差可能会导致闭环不稳定。因此,不建议将Smith预测器用于运行时不确定的延迟运行系统。对使用两个替代pH传感器的弱酸/强碱中和控制系统进行了建模和分析。第一个传感器是一个传统的pH电极,其输出信号与pH成正比,第二个传感器是一个光纤光极,其产生的信号与氢离子浓度成正比。系统仿真研究表明,在反馈回路中使用光极代替电极传感器时,没有观察到固有的性能改善。

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