TY - JOUR
T1 - A novel control strategy for enhancing biological N-removal in a granular sequencing batch reactor
T2 - A model-based study
AU - Isanta, Eduardo
AU - Figueroa, Mónica
AU - Mosquera-Corral, Anuska
AU - Campos, Luis
AU - Carrera, Julián
AU - Pérez, Julio
N1 - Funding Information:
This work has been supported by the Spanish Ministerio de Economía y Competitividad through GRANMADEL/TOGRANSYS Project (CTQ2008-06792-C02-02/PPQ) and ONLYBIO Project (CTQ2011-24745/PPQ).
PY - 2013/10
Y1 - 2013/10
N2 - Biological nitrogen removal in aerobic granular sequencing batch reactors is sensitively affected by process conditions (e.g. dissolved oxygen (DO) concentration, nitrogen loading rate (NLR), influent C/N ratio, among others). The variation of one of these process conditions affects the others, because often they are tightly linked. These interrelationships are a drawback for the experimental assessment of the target domain of process conditions required to enhance N-removal. Here, we have developed a model to determine the guidelines to design an automatic control strategy with the final aim of enhancing biological N-removal in a granular sequencing batch reactor. The model was first calibrated with experimental data from a granular sequencing batch reactor treating swine wastewater. Specific simulations were designed to elucidate the effect of DO concentration (0.5-8mgO2L-1), granule size (0.5-3.5mm), influent C/N ratio (4-10gO2g-1N) and NLR (0.41-0.82gNL-1d-1) on the nitrification-denitrification efficiency. Simulation results showed that, in general, high N-removal efficiencies (from 70% to 85%) could be obtained only setting the appropriate DO concentration. That appropriate DO concentration could be easily found based on effluent ammonium concentration. Those results were used to propose a control strategy to enhance N-removal efficiencies. The control strategy was based on a closed DO loop with variable DO set-point. The DO set-point was established at a constant value for the whole cycle (i.e. once per cycle), based on the on-line measurement of ammonium concentration at the end of the previous cycle.
AB - Biological nitrogen removal in aerobic granular sequencing batch reactors is sensitively affected by process conditions (e.g. dissolved oxygen (DO) concentration, nitrogen loading rate (NLR), influent C/N ratio, among others). The variation of one of these process conditions affects the others, because often they are tightly linked. These interrelationships are a drawback for the experimental assessment of the target domain of process conditions required to enhance N-removal. Here, we have developed a model to determine the guidelines to design an automatic control strategy with the final aim of enhancing biological N-removal in a granular sequencing batch reactor. The model was first calibrated with experimental data from a granular sequencing batch reactor treating swine wastewater. Specific simulations were designed to elucidate the effect of DO concentration (0.5-8mgO2L-1), granule size (0.5-3.5mm), influent C/N ratio (4-10gO2g-1N) and NLR (0.41-0.82gNL-1d-1) on the nitrification-denitrification efficiency. Simulation results showed that, in general, high N-removal efficiencies (from 70% to 85%) could be obtained only setting the appropriate DO concentration. That appropriate DO concentration could be easily found based on effluent ammonium concentration. Those results were used to propose a control strategy to enhance N-removal efficiencies. The control strategy was based on a closed DO loop with variable DO set-point. The DO set-point was established at a constant value for the whole cycle (i.e. once per cycle), based on the on-line measurement of ammonium concentration at the end of the previous cycle.
KW - Aerobic granular sludge
KW - Dissolved oxygen concentration
KW - Mathematical modeling
KW - Nitrification-denitrification
KW - On-line ammonium concentration
KW - Particle size
UR - http://www.scopus.com/inward/record.url?scp=84883387071&partnerID=8YFLogxK
U2 - 10.1016/j.cej.2013.07.118
DO - 10.1016/j.cej.2013.07.118
M3 - Article
AN - SCOPUS:84883387071
SN - 1385-8947
VL - 232
SP - 468
EP - 477
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
ER -