Model-based optimization of a sequencing batch reactor for biological nitrogen removal.
An optimal operating mode for a sequencing batch reactor was determined via a model-based optimization. Synthetic wastewater containing mainly organic matter (as glucose) and nitrogen (as ammonium chloride) was treated without any addition of an external carbon source to accomplish denitrification step. A simplified model was used to describe process dynamics, comprised of six ordinary differential equations and an empirical correlation for oxygen consumption rate. Batch cycle time was the chosen objective function to be minimized for a fixed volume of waste to be treated. Furthermore, as SBR operation is divided in two major phases - aerobic and anoxic, to achieve total pollutants removal within minimum time, these phases can be repeatedly alternated. To ensure availability of organic matter necessary for denitrification, these two phases were combined with feed steps. Different feed strategies were tested using one, two or three feed steps. A successive quadratic programming algorithm was used, and maximum values for final COD, nitrate and ammonium concentrations, as well as maximum feed pump flow rate were some the process constraints. One step feed strategy was indicated by the optimization leading to a batch cycle time of 5h.
Escola de Química, Universidade Federal do Rio de Janeiro, CT, Bl.E, Lab. 113, Cidade Universitária, 21949-900 Rio de Janeiro-RJ, Brazil.
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D000332:Aerobiosis; D000693:Anaerobiosis; D018533:Biomass; D019149:Bioreactors; D004867:Equipment Design; D007700:Kinetics; D008954:Models, Biological; D009584:Nitrogen / Q000302:isolation & purification*; D009930:Organic Chemicals / Q000032:analysis; D010100:Oxygen / Q000032:analysis; D000644:Quaternary Ammonium Compounds / Q000032:analysis; D014865:Waste Disposal, Fluid / Q000295:instrumentation / Q000379:methods*
D009930:Organic Chemicals; D000644:Quaternary Ammonium Compounds; D009584:Nitrogen; D010100:Oxygen