title: New generic mathematical model for WWTP sludge digesters operating under aerobic and anaerobic conditions: Model building and experimental verification.
abstract: This paper presents a new mathematical model developed to reproduce the performance of a generic sludge digester working either under aerobic or anaerobic operational conditions. The digester has been modelled as two completely mixed tanks associated with gaseous and liquid volumes. The conversion model has been developed based on a plant wide modelling methodology (PWM) and comprises biochemical transformations, physicochemical reactions and thermodynamic considerations. The model predicts the reactor temperature and the temporary evolution of an extensive vector of model components which are completely defined in terms of elemental mass fractions (C, H, O, N and P) and charge density. Thus, the comprehensive definition of the model components guarantees the continuity of elemental mass and charge in all the model transformations and between any two systems defined by the model. The aim of the generic digester model is to overcome the problems that arise when trying to connect aerobic and anaerobic digestion processes working in series or to connect water and sludge lines in a WWTP. The modelling methodology used has allowed the systematic construction of the biochemical model which acts as an initial illustrative example of an application that has been experimentally verified. The variation of the temperature is also predicted based on a thermal dynamic model. Real data from four different facilities and a straightforward calibration have been used to successfully verify the model predictions in the cases of mesophilic and thermophilic anaerobic digestion as well as autothermal thermophilic aerobic digestion (ATAD). The large amount of data from the full scale ATAD and the anaerobic digestion pilot plants, all of them working under different conditions, has allowed the validation of the model for that case study.
authors.affiliation: CEIT, Section of Environmental Engineering, San Sebastián, Spain. mdegracia@atmsa.com
authors.forename: M
authors.initials: M
authors.lastname: de Gracia
authors.forename: P
authors.initials: P
authors.lastname: Grau
authors.forename: E
authors.initials: E
authors.lastname: Huete
authors.forename: J
authors.initials: J
authors.lastname: Gómez
authors.forename: J L
authors.initials: JL
authors.lastname: García-Heras
authors.forename: E
authors.initials: E
authors.lastname: Ayesa
mesh_terms: D000332:Aerobiosis; D000465:Algorithms; D000693:Anaerobiosis; D001420:Bacteria, Aerobic / Q000254:growth & development / Q000378:metabolism; D001421:Bacteria, Anaerobic / Q000254:growth & development / Q000378:metabolism; D001673:Biodegradation, Environmental; D019149:Bioreactors / Q000382:microbiology; D008962:Models, Theoretical; D012722:Sewage / Q000737:chemistry* / Q000382:microbiology; D013816:Thermodynamics; D014865:Waste Disposal, Fluid / Q000379:methods*; D018508:Water Purification / Q000379:methods
chemical_list: D012722:Sewage