TY - JOUR
T1 - Modelling aerobic granular SBR at variable COD/N ratios including accurate description of total solids concentration
AU - Vázquez-Padín, José Ramón
AU - Mosquera-Corral, Anuska
AU - Campos, José Luis
AU - Méndez, Ramón
AU - Carrera, Julián
AU - Pérez, Julio
N1 - Funding Information:
This work was funded by the Spanish Government (TOGRANSYS coordinated project CTQ2008-06792-C02/PPQ and NOVEDAR_Consolider CSD2007-00055). J.R. Vázquez-Padín wants to thank the Spanish Ministry of Education and Science for his FPU grant. Julio Pérez and Julián Carrera are members of the GENOCOV group (Grup de Recerca Consolidat de la Generalitat de Catalunya, 2009-SGR-815). Funding from the Autonomous University of Barcelona (program EME2004-40) is gratefully acknowledged.
PY - 2010/4/15
Y1 - 2010/4/15
N2 - The operation of a sequencing batch reactor (SBR) with aerobic granular biomass was successfully simulated using a one-dimensional biofilm model. The biological processes considered were described based on the activated sludge model (ASM) platform with two main modifications: (i) simultaneous growth and storage of organic substrates by heterotrophic bacteria; and (ii) inclusion of nitrite as intermediate compound in the nitrification and denitrification processes. Three different operational conditions were evaluated, characterized by different chemical oxygen demand to nitrogen (COD/N) ratios in the influent of: 0, 1.25 and 5.5 kg kg-1, representing a purely autotrophic media and two heterotrophic media, respectively. An accurate description of the experimental concentrations of COD, ammonium, nitrite, nitrate, dissolved oxygen (DO) and alkalinity along the cycles was obtained. Total solids concentration inside the reactor (5.0, 2.0 and 1.0 kg VSS m-3 for (COD/N) ratio of 5.5, 1.25 and 0 kg kg-1, respectively) and biofilm density (23 kg mgranule- 3) were correctly described with the model. To obtain an accurate description of both solids concentration and biofilm density different densities were defined for the particulate compounds and a porosity profile along the granule was imposed. Oxygen penetration depths obtained with the model were 0.35 × 10-3, 0.30 × 10-3 and 0.12 × 10-3 m for (COD/N) ratio of 5.5, 1.25 and 0 kg kg-1, respectively. The values were in agreement with those used in the description of the porosity profiles.
AB - The operation of a sequencing batch reactor (SBR) with aerobic granular biomass was successfully simulated using a one-dimensional biofilm model. The biological processes considered were described based on the activated sludge model (ASM) platform with two main modifications: (i) simultaneous growth and storage of organic substrates by heterotrophic bacteria; and (ii) inclusion of nitrite as intermediate compound in the nitrification and denitrification processes. Three different operational conditions were evaluated, characterized by different chemical oxygen demand to nitrogen (COD/N) ratios in the influent of: 0, 1.25 and 5.5 kg kg-1, representing a purely autotrophic media and two heterotrophic media, respectively. An accurate description of the experimental concentrations of COD, ammonium, nitrite, nitrate, dissolved oxygen (DO) and alkalinity along the cycles was obtained. Total solids concentration inside the reactor (5.0, 2.0 and 1.0 kg VSS m-3 for (COD/N) ratio of 5.5, 1.25 and 0 kg kg-1, respectively) and biofilm density (23 kg mgranule- 3) were correctly described with the model. To obtain an accurate description of both solids concentration and biofilm density different densities were defined for the particulate compounds and a porosity profile along the granule was imposed. Oxygen penetration depths obtained with the model were 0.35 × 10-3, 0.30 × 10-3 and 0.12 × 10-3 m for (COD/N) ratio of 5.5, 1.25 and 0 kg kg-1, respectively. The values were in agreement with those used in the description of the porosity profiles.
KW - Aerobic granulation
KW - Biomass density
KW - Mass transfer
KW - Microbial kinetics
KW - Solids concentration
KW - Wastewater treatment
UR - http://www.scopus.com/inward/record.url?scp=77549087410&partnerID=8YFLogxK
U2 - 10.1016/j.bej.2009.12.009
DO - 10.1016/j.bej.2009.12.009
M3 - Article
AN - SCOPUS:77549087410
SN - 1369-703X
VL - 49
SP - 173
EP - 184
JO - Biochemical Engineering Journal
JF - Biochemical Engineering Journal
IS - 2
ER -