Multivariable PID control of an Activated Sludge Wastewater Treatment Process

In general, wastewater treatment plant (WWTP) consists of several stages before it is released to a receiving water body. There are, preliminary and primary treatment (mechanical treatment), a secondary treatment (biological treatment) and a tertiary treatment (chemical treatment). In this chapter, since the work involve of identification and control design of activated sludge process to improve the performance of the system, and most of the control priorities are centred on the biological treatment process, only the secondary treatment will be highlighted.

[1]  Martin Cote,et al.  Dynamic modelling of the activated sludge process: Improving prediction using neural networks , 1995 .

[2]  W. Gujer,et al.  Activated sludge model No. 3 , 1995 .

[3]  E. Bristol On a new measure of interaction for multivariable process control , 1966 .

[4]  Michel Verhaegen,et al.  Identification of the deterministic part of MIMO state space models given in innovations form from input-output data , 1994, Autom..

[5]  Petre Stoica,et al.  Decentralized Control , 2018, The Control Systems Handbook.

[6]  I. Takács A dynamic model of the clarification-thickening process , 1991 .

[7]  Heikki N. Koivo,et al.  Multivariable tuning regulators for unknown systems , 1980, Autom..

[8]  Michel Kinnaert,et al.  Interaction measures and pairing of controlled and manipulated variables for multiple-input-multiple-output systems: a survey , 1995 .

[9]  M. Moonen,et al.  On- and off-line identification of linear state-space models , 1989 .

[10]  Sylvie Gillot,et al.  The COST Simulation Benchmark: Description and Simulator Manual , 2001 .

[11]  Ian T. Cameron,et al.  Analysis of dynamic process models for structural insight and model reduction—Part 1. Structural identification measures , 1997 .

[12]  Mikael Andersson,et al.  Control of the aeration volume in an activated sludge process using supervisory control strategies. , 2006, Water research.

[13]  Maciejowsk Multivariable Feedback Design , 1989 .

[14]  Ahmed Gamal el-Din,et al.  A combined transfer-function noise model to predict the dynamic behavior of a full-scale primary sedimentation tank. , 2002, Water research.

[15]  N Hvala,et al.  Comparison of control strategies for nitrogen removal in an activated sludge process in terms of operating costs: a simulation study. , 2007, Water research.

[16]  Ma Yong,et al.  Feedforward-feedback control of dissolved oxygen concentration in a predenitrification system , 2005, Bioprocess and biosystems engineering.

[17]  Robert Piotrowski,et al.  LOWER – LEVEL CONTROLLER FOR HIERARCHICAL CONTROL OF DISSOLVED OXYGEN CONCENTRATION IN ACTIVATED SLUDGE PROCESSES , 2005 .

[18]  Mietek A. Brdys,et al.  Dissolved Oxygen Control for Activated Sludge Processes , 2001 .