Control of the aeration volume in an activated sludge process using supervisory control strategies.

In this paper, a simulation benchmark of a pre-denitrifying activated sludge process is utilized in order to evaluate a supervisory aeration volume control strategy. The aeration volume control strategy has also been evaluated in a pilot plant at Hammarby Sjöstad in Stockholm, Sweden. The main idea has been to let the dissolved oxygen (DO) concentration in some of the aerated compartments be determined by a higher level controller driven by the DO concentration in other compartments. In this way, only sensors for measuring the DO concentrations are needed for the decision of time varying DO set-points. The high reliability of such sensors implies robust input values for the proposed control strategy. Moreover, it is known that the respiration rate is affected by the content of substrate and nitrogen in the compartments; therefore, the suggested manipulations of the DO set-points are indirectly determined by the current load into the plant. Compared to constant DO control and a supervisory DO set-point control strategy based on ammonium measurements in the last aerobic compartment, the suggested aeration volume control strategy could reduce the effluent nitrate and ammonium concentrations significantly without increasing the aeration energy.

[1]  Mogens Henze,et al.  Wastewater Treatment: Biological and Chemical Processes , 1995 .

[2]  D. Vrecko,et al.  Improvement of ammonia removal in activated sludge process with feedforward-feedback aeration controllers. , 2006, Water science and technology : a journal of the International Association on Water Pollution Research.

[3]  A. Ekster Automatic waste control , 1998 .

[4]  B Carlsson,et al.  Control of an activated sludge process with nitrogen removal--a benchmark study. , 2002, Water science and technology : a journal of the International Association on Water Pollution Research.

[5]  G. Olsson,et al.  A hedging point strategy--balancing effluent quality, economy and robustness in the control of wastewater treatment plants. , 2002, Water science and technology : a journal of the International Association on Water Pollution Research.

[6]  K. Hoen,et al.  Control of nitrogen removal in wastewater treatment plants with predenitrification, depending on the actual purification capacity , 1996 .

[7]  J. Alex,et al.  PREDICTIVE CONTROL OF NITROGEN REMOVAL IN WWTPS USING PARSIMONIOUS MODELS , 2002 .

[8]  B Carlsson,et al.  Control of the aeration volume in an activated sludge process for nitrogen removal. , 2002, Water science and technology : a journal of the International Association on Water Pollution Research.

[9]  Bram Klapwijk,et al.  Feedforward control of nitrification by manipulating the aerobic volume in activated sludge plants , 1998 .

[10]  Carl-Fredrik Lindberg,et al.  Control and estimation strategies applied to the activated sludge process , 1997 .

[11]  M. N. Pons,et al.  Benchmark for evaluating control strategies in wastewater treatment plants , 1999, 1999 European Control Conference (ECC).

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

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

[14]  M. Nielsen,et al.  Optimization of a nitrogen-removing biological wastewater treatment plant using on-line measurements , 1994 .