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前置反硝化系统中溶解氧浓度的前馈-反馈控制

Feedforward-feedback control of dissolved oxygen concentration in a predenitrification system.

作者信息

Yong Ma, Yongzhen Peng, Shuying Wang

机构信息

School of Municipal and Environmental Engineering, Harbin Institute of Technology, Harbin, Box 2607, 150090, China.

出版信息

Bioprocess Biosyst Eng. 2005 Jul;27(4):223-8. doi: 10.1007/s00449-004-0390-0. Epub 2005 May 18.

Abstract

As the largest single energy-consuming component in most biological wastewater treatment systems, aeration control is of great interest from the point of view of saving energy and improving wastewater treatment plant efficiency. In this paper, three different strategies, including conventional constant dissolved oxygen (DO) set-point control, cascade DO set-point control, and feedforward-feedback DO set-point control were evaluated using the denitrification layout of the IWA simulation benchmark. Simulation studies showed that the feedforward-feedback DO set-point control strategy was better than the other control strategies at meeting the effluent standards and reducing operational costs. The control strategy works primarily by feedforward control based on an ammonium sensor located at the head of the aerobic process. It has an important advantage over effluent measurements in that there is no (or only a very short) time delay for information; feedforward control was combined with slow feedback control to compensate for model approximations. The feedforward-feedback DO control was implemented in a lab-scale wastewater treatment plant for a period of 60 days. Compared to operation with constant DO concentration, the required airflow could be reduced by up to 8-15% by employing the feedforward-feedback DO-control strategy, and the effluent ammonia concentration could be reduced by up to 15-25%. This control strategy can be expected to be accepted by the operating personnel in wastewater treatment plants.

摘要

作为大多数生物废水处理系统中最大的单一能耗组件,从节能和提高废水处理厂效率的角度来看,曝气控制备受关注。本文采用国际水协模拟基准的反硝化布局,对三种不同策略进行了评估,包括传统的恒定溶解氧(DO)设定值控制、串级DO设定值控制和前馈-反馈DO设定值控制。模拟研究表明,在前馈-反馈DO设定值控制策略在满足出水标准和降低运营成本方面优于其他控制策略。该控制策略主要通过基于位于好氧工艺前端的铵传感器进行前馈控制来实现。与出水测量相比,它具有一个重要优势,即信息不存在(或只有非常短的)时间延迟;前馈控制与慢速反馈控制相结合,以补偿模型近似值。前馈-反馈DO控制在实验室规模的废水处理厂中实施了60天。与恒定DO浓度运行相比,采用前馈-反馈DO控制策略可将所需气流减少多达8-15%,出水氨浓度可降低多达15-25%。预计这种控制策略会被废水处理厂的操作人员所接受。

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