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Application of the General Model "Biological Nutrient Removal Model No.1" to upgrade two full-scale WWTPs

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Application of the General Model "Biological Nutrient Removal Model No.1" to upgrade two full-scale WWTPs

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dc.contributor.author Ruano García, María Victoria es_ES
dc.contributor.author Serralta Sevilla, Joaquín es_ES
dc.contributor.author Ribes Bertomeu, Jose es_ES
dc.contributor.author García Usach, Mª Francisca es_ES
dc.contributor.author Bouzas Blanco, Alberto es_ES
dc.contributor.author Barat Baviera, Ramón es_ES
dc.contributor.author Seco Torrecillas, Aurora es_ES
dc.contributor.author Ferrer Polo, José es_ES
dc.date.accessioned 2014-01-15T12:32:08Z
dc.date.issued 2012-05
dc.identifier.issn 0959-3330
dc.identifier.uri http://hdl.handle.net/10251/34919
dc.description.abstract In this paper, two practical case studies for upgrading two wastewater treatment plants (WWTPs) using the general model BNRM1 (Biological Nutrient Removal Model No. 1) are presented. In the first case study, the Tarragona WWTP was upgraded by reducing the phosphorus load to the anaerobic digester in order to minimize the precipitation problems. Phosphorus load reduction was accomplished by mixing the primary sludge and the secondary sludge and by elutriating the mixed sludge. In the second case study, the Alcantarilla WWTP, the nutrient removal was enhanced by maintaining a relatively low dissolved oxygen concentration in Stage A to maintain the acidogenic bacteria activity. The VFA produced in Stage A favour the denitrification process and biological phosphorus removal in Stage B. These case studies demonstrate the benefits of using the general model BNRM1 to simulate settling processes and biological processes related to both anaerobic and aerobic bacteria in the same process unit. es_ES
dc.description.sponsorship The authors would like to express their gratitude to the Ministry of Science and Education (Spain) for their financial support (CTM2005-06919-C03.). Financial support from Entitat Publica de Sanejament d'Aigues Residuals de la Comunitat Valenciana and Depuracion de Aguas del Mediterraneo is also gratefully acknowledged. en_EN
dc.format.extent 8 es_ES
dc.language Inglés es_ES
dc.publisher Taylor & Francis: STM, Behavioural Science and Public Health Titles es_ES
dc.relation.ispartof Environmental Technology es_ES
dc.rights Reserva de todos los derechos es_ES
dc.subject Activated sludge models es_ES
dc.subject Biological nutrient removal es_ES
dc.subject BNRM1 es_ES
dc.subject Plant-wide mathematical modelling es_ES
dc.subject WWTP upgrading es_ES
dc.subject WATER TREATMENT PLANTS es_ES
dc.subject ACTIVATED-SLUDGE MODEL es_ES
dc.subject WASTE-WATER es_ES
dc.subject CALIBRATION es_ES
dc.subject SIMULATION es_ES
dc.subject ASM2D es_ES
dc.subject.classification TECNOLOGIA DEL MEDIO AMBIENTE es_ES
dc.title Application of the General Model "Biological Nutrient Removal Model No.1" to upgrade two full-scale WWTPs es_ES
dc.type Artículo es_ES
dc.embargo.lift 10000-01-01
dc.embargo.terms forever es_ES
dc.identifier.doi 10.1080/09593330.2011.604877
dc.relation.projectID info:eu-repo/grantAgreement/MEC//CTM2005-06919-C03-02/ES/ESTUDIO DE TECNICAS AVANZADAS DE ELIMINACION DE NITROGENO EN CORRIENTES CON ELEVADAS CONCENTRACIONES DE NITROGENO AMONIACAL/ es_ES
dc.relation.projectID info:eu-repo/grantAgreement/MEC//CTM2005-06919-C03-01/ES/MODELACIÓN DE LOS PROCESOS IMPLICADOS EN LA ELIMINACION DE NITROGENO EN EL SOBRENADANTE DE LA DESHIDRATACION DE FANGOS/ es_ES
dc.rights.accessRights Cerrado es_ES
dc.contributor.affiliation Universitat Politècnica de València. Departamento de Ingeniería Hidráulica y Medio Ambiente - Departament d'Enginyeria Hidràulica i Medi Ambient es_ES
dc.contributor.affiliation Universitat Politècnica de València. Instituto Universitario de Ingeniería del Agua y del Medio Ambiente - Institut Universitari d'Enginyeria de l'Aigua i Medi Ambient es_ES
dc.description.bibliographicCitation Ruano García, MV.; Serralta Sevilla, J.; Ribes Bertomeu, J.; García Usach, MF.; Bouzas Blanco, A.; Barat Baviera, R.; Seco Torrecillas, A.... (2012). Application of the General Model "Biological Nutrient Removal Model No.1" to upgrade two full-scale WWTPs. Environmental Technology. 33(9):1005-1012. https://doi.org/10.1080/09593330.2011.604877 es_ES
dc.description.accrualMethod S es_ES
dc.relation.publisherversion http://dx.doi.org/10.1080/09593330.2011.604877 es_ES
dc.description.upvformatpinicio 1005 es_ES
dc.description.upvformatpfin 1012 es_ES
dc.type.version info:eu-repo/semantics/publishedVersion es_ES
dc.description.volume 33 es_ES
dc.description.issue 9 es_ES
dc.relation.senia 191872
dc.identifier.eissn 1479-487X
dc.contributor.funder Ministerio de Educación y Ciencia es_ES
dc.contributor.funder Entitat Pública de Sanejament d'Aigües Residuals de la Comunitat Valenciana es_ES
dc.contributor.funder Depuración de Aguas del Mediterráneo, S.L. es_ES
dc.description.references Gernaey, K. V., van Loosdrecht, M. C. ., Henze, M., Lind, M., & Jørgensen, S. B. (2004). Activated sludge wastewater treatment plant modelling and simulation: state of the art. Environmental Modelling & Software, 19(9), 763-783. doi:10.1016/j.envsoft.2003.03.005 es_ES
dc.description.references Ferrer, J., Seco, A., Serralta, J., Ribes, J., Manga, J., Asensi, E., … Llavador, F. (2008). DESASS: A software tool for designing, simulating and optimising WWTPs. Environmental Modelling & Software, 23(1), 19-26. doi:10.1016/j.envsoft.2007.04.005 es_ES
dc.description.references Ferrer, J., Morenilla, J. J., Bouzas, A., & Garcia-Usach, F. (2004). Calibration and simulation of two large wastewater treatment plants operated for nutrient removal. Water Science and Technology, 50(6), 87-94. doi:10.2166/wst.2004.0363 es_ES
dc.description.references Derbal, K., Bencheikh-lehocine, M., Cecchi, F., Meniai, A.-H., & Pavan, P. (2009). Application of the IWA ADM1 model to simulate anaerobic co-digestion of organic waste with waste activated sludge in mesophilic condition. Bioresource Technology, 100(4), 1539-1543. doi:10.1016/j.biortech.2008.07.064 es_ES
dc.description.references Ruano, M. V., Ribes, J., Seco, A., & Ferrer, J. (2011). DSC: software tool for simulation-based design of control strategies applied to wastewater treatment plants. Water Science and Technology, 63(4), 796-803. doi:10.2166/wst.2011.311 es_ES
dc.description.references Seco, A., Ribes, J., Serralta, J., & Ferrer, J. (2004). Biological nutrient removal model No.1 (BNRM1). Water Science and Technology, 50(6), 69-70. doi:10.2166/wst.2004.0361 es_ES
dc.description.references Seco, A., Ferrer, J., Serralta, J., Ribes, J., Barat, R., & Bouzas, A. (2004). Use of Biological and Sedimentation Models for Designing Peñíscola WWTP. Environmental Technology, 25(6), 681-687. doi:10.1080/09593330.2004.9619358 es_ES
dc.description.references Serralta, J., Ribes, J., Seco, A., & Ferrer, J. (2002). A supervisory control system for optimising nitrogen removal and aeration energy consumption in wastewater treatment plants. Water Science and Technology, 45(4-5), 309-316. doi:10.2166/wst.2002.0612 es_ES
dc.description.references Activated Sludge Model No.2d, ASM2d. (1999). Water Science and Technology, 39(1). doi:10.1016/s0273-1223(98)00829-4 es_ES
dc.description.references Satoh, H., Okuda, E., Mino, T., & Matsuo, T. (2000). Calibration of kinetic parameters in the IAWQ Activated Sludge Model: a pilot scale experience. Water Science and Technology, 42(3-4), 29-34. doi:10.2166/wst.2000.0355 es_ES
dc.description.references Serralta, J., Ferrer, J., Borrás, L., & Seco, A. (2004). An extension of ASM2d including pH calculation. Water Research, 38(19), 4029-4038. doi:10.1016/j.watres.2004.07.009 es_ES
dc.description.references TAKACS, I. (1991). A dynamic model of the clarification-thickening process. Water Research, 25(10), 1263-1271. doi:10.1016/0043-1354(91)90066-y es_ES
dc.description.references Ribes, J., Ferrer, J., Bouzas, A., & Seco, A. (2002). Modelling of an Activated Primary Settling Tank Including the Fermentation Process and VFA Elutriation. Environmental Technology, 23(10), 1147-1156. doi:10.1080/09593332308618333 es_ES
dc.description.references Barat, R., Bouzas, A., Martí, N., Ferrer, J., & Seco, A. (2009). Precipitation assessment in wastewater treatment plants operated for biological nutrient removal: A case study in Murcia, Spain. Journal of Environmental Management, 90(2), 850-857. doi:10.1016/j.jenvman.2008.02.001 es_ES
dc.description.references Pastor, L., Marti, N., Bouzas, A., & Seco, A. (2008). Sewage sludge management for phosphorus recovery as struvite in EBPR wastewater treatment plants. Bioresource Technology, 99(11), 4817-4824. doi:10.1016/j.biortech.2007.09.054 es_ES
dc.description.references Penya-Roja, J. M., Seco, A., Ferrer, J., & Serralta, J. (2002). Calibration and Validation of Activated Sludge Model No.2d for Spanish Municipal Wastewater. Environmental Technology, 23(8), 849-862. doi:10.1080/09593332308618360 es_ES


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