Economic and environmental feasibility assessment of two different AnMBR-based treatment schemes treating sulfate-rich urban wastewater
[EN] Two different facilities with AnMBR technology for sulfate-rich wastewater are analyzed. Scenario 1 consists of an AnMBR fed with raw wastewater. Scenario 2 couples AnMBR, primary settling and anaerobic digestion. Scenarios 1 and 2 were simulated with DESASS 7.1 software considering experimenta...
| Autores: | , , , , |
|---|---|
| Formato: | artículo |
| Fecha de publicación: | 2025 |
| País: | España |
| Recursos: | Universitat Politècnica de València (UPV) |
| Repositorio: | RiuNet. Repositorio Institucional de la Universitat Politécnica de Valéncia |
| Idioma: | inglés |
| OAI Identifier: | oai:riunet.upv.es:10251/220370 |
| Acesso em linha: | https://riunet.upv.es/handle/10251/220370 |
| Access Level: | acceso embargado |
| Palavra-chave: | AnMBR Resource recovery LCC LCA Sulfate-rich municipal wastewater |
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Economic and environmental feasibility assessment of two different AnMBR-based treatment schemes treating sulfate-rich urban wastewaterMateo, O.Jiménez-Benítez, A.Robles, A.Martí, N.Serralta Sevilla, Joaquín|||0000-0001-5015-0689AnMBRResource recoveryLCCLCASulfate-rich municipal wastewater[EN] Two different facilities with AnMBR technology for sulfate-rich wastewater are analyzed. Scenario 1 consists of an AnMBR fed with raw wastewater. Scenario 2 couples AnMBR, primary settling and anaerobic digestion. Scenarios 1 and 2 were simulated with DESASS 7.1 software considering experimental data obtained from an AnMBR demonstration plant located in Carraixet facility (Valencia, Spain). Comparison between both scenarios is made based on their energy balances and applying the life cycle costing and life cycle assessment methodologies. Energy results showed net energy consumption of 0.148 kWh center dot m-3 in scenario 1 and a net energy savings of 0.057 kWh center dot m-3 in scenario 2 due to reduced mixing requirement and improved energy recovery. Energy savings also allows reducing operating expenditure in scenario 2 (0.022 m-3) compared to scenario 1 (0.066 m-3). Degassing membranes in scenario 1 (0.020 m-3) also contribute to increase its capital expenditure (0.083 m-3) over scenario 2 (0.055 m-3). Scenario 2 shows a better environmental performance in all the categories evaluated. The absence of dissolved methane in the effluent and the improved energy recovery allowed scenario 2 to act as carbon sink (-0.033 kgCO2eq center dot m-3). Therefore, coupling AnMBR, primary settling and anaerobic digestion improves the feasibility of sulfate-rich wastewater treatments compared to AnMBR alone.The authors would like to acknowledge the Ministry of Science and Innovation for supporting the project "RECREATE" (PID2020-114315RB-C22) and "BIONUTEN" (CTM2014-54980-C2-R) where this research is framed and the Ministry of Universities for the financial research fellowship of the first author (BES-2015-073403) .ElsevierDepartamento de Ingeniería Hidráulica y Medio AmbienteInstituto Universitario de Ingeniería del Agua y del Medio AmbienteEscuela Técnica Superior de Ingeniería de Caminos, Canales y PuertosAgencia Estatal de InvestigaciónMinisterio de Economía y CompetitividadRepositorio Institucional de la Universitat Politècnica de València Riunet20252025-04-0120252025-04-0820272027-02-28journal articlehttp://purl.org/coar/resource_type/c_6501VoRhttp://purl.org/coar/version/c_970fb48d4fbd8a85info:eu-repo/semantics/articleapplication/pdfapplication/pdfhttps://riunet.upv.es/handle/10251/220370reponame:RiuNet. Repositorio Institucional de la Universitat Politécnica de Valénciainstname:Universitat Politècnica de València (UPV)InglésengAgencia Estatal de Investigación http://dx.doi.org/10.13039/501100011033 Plan Estatal de Investigación Científica y Técnica y de Innovación 2017-2020 PID2020-114315RB-C22 ESTUDIO DE TECNOLOGIAS PARA LA RECUPERACION DE NUTRIENTES DE LAS CORRIENTES OBTENIDAS EN INSTALACIONES DE RECUPERACION DE RECURSOS CON CARBONIZACION HIDROTERMAL DE LODOS.Ministerio de Economía y Competitividad http://dx.doi.org/10.13039/501100003329 BES-2015-073403 BES-2015-073403Ministerio de Economía y Competitividad http://dx.doi.org/10.13039/501100003329 CTM2014-54980-C2-1-R OBTENCION DE BIONUTRIENTES Y ENERGIA DEL AGUA RESIDUAL URBANA MEDIANTE CULTIVO DE MICROALGAS, TRATAMIENTOS ANAEROBIOS, CRISTALIZACION DE FOSFORO, ABSORCION DE NH3 Y COMPOSTAJEembargoed accesshttp://purl.org/coar/access_right/c_f1cfReconocimiento - No comercial - Sin obra derivada (by-nc-nd) http://creativecommons.org/licenses/by-nc-nd/4.0/info:eu-repo/semantics/embargoedAccessoai:riunet.upv.es:10251/2203702026-06-13T07:49:27Z |
| dc.title.none.fl_str_mv |
Economic and environmental feasibility assessment of two different AnMBR-based treatment schemes treating sulfate-rich urban wastewater |
| title |
Economic and environmental feasibility assessment of two different AnMBR-based treatment schemes treating sulfate-rich urban wastewater |
| spellingShingle |
Economic and environmental feasibility assessment of two different AnMBR-based treatment schemes treating sulfate-rich urban wastewater Mateo, O. AnMBR Resource recovery LCC LCA Sulfate-rich municipal wastewater |
| title_short |
Economic and environmental feasibility assessment of two different AnMBR-based treatment schemes treating sulfate-rich urban wastewater |
| title_full |
Economic and environmental feasibility assessment of two different AnMBR-based treatment schemes treating sulfate-rich urban wastewater |
| title_fullStr |
Economic and environmental feasibility assessment of two different AnMBR-based treatment schemes treating sulfate-rich urban wastewater |
| title_full_unstemmed |
Economic and environmental feasibility assessment of two different AnMBR-based treatment schemes treating sulfate-rich urban wastewater |
| title_sort |
Economic and environmental feasibility assessment of two different AnMBR-based treatment schemes treating sulfate-rich urban wastewater |
| dc.creator.none.fl_str_mv |
Mateo, O. Jiménez-Benítez, A. Robles, A. Martí, N. Serralta Sevilla, Joaquín|||0000-0001-5015-0689 |
| author |
Mateo, O. |
| author_facet |
Mateo, O. Jiménez-Benítez, A. Robles, A. Martí, N. Serralta Sevilla, Joaquín|||0000-0001-5015-0689 |
| author_role |
author |
| author2 |
Jiménez-Benítez, A. Robles, A. Martí, N. Serralta Sevilla, Joaquín|||0000-0001-5015-0689 |
| author2_role |
author author author author |
| dc.contributor.none.fl_str_mv |
Departamento de Ingeniería Hidráulica y Medio Ambiente Instituto Universitario de Ingeniería del Agua y del Medio Ambiente Escuela Técnica Superior de Ingeniería de Caminos, Canales y Puertos Agencia Estatal de Investigación Ministerio de Economía y Competitividad Repositorio Institucional de la Universitat Politècnica de València Riunet |
| dc.subject.none.fl_str_mv |
AnMBR Resource recovery LCC LCA Sulfate-rich municipal wastewater |
| topic |
AnMBR Resource recovery LCC LCA Sulfate-rich municipal wastewater |
| description |
[EN] Two different facilities with AnMBR technology for sulfate-rich wastewater are analyzed. Scenario 1 consists of an AnMBR fed with raw wastewater. Scenario 2 couples AnMBR, primary settling and anaerobic digestion. Scenarios 1 and 2 were simulated with DESASS 7.1 software considering experimental data obtained from an AnMBR demonstration plant located in Carraixet facility (Valencia, Spain). Comparison between both scenarios is made based on their energy balances and applying the life cycle costing and life cycle assessment methodologies. Energy results showed net energy consumption of 0.148 kWh center dot m-3 in scenario 1 and a net energy savings of 0.057 kWh center dot m-3 in scenario 2 due to reduced mixing requirement and improved energy recovery. Energy savings also allows reducing operating expenditure in scenario 2 (0.022 m-3) compared to scenario 1 (0.066 m-3). Degassing membranes in scenario 1 (0.020 m-3) also contribute to increase its capital expenditure (0.083 m-3) over scenario 2 (0.055 m-3). Scenario 2 shows a better environmental performance in all the categories evaluated. The absence of dissolved methane in the effluent and the improved energy recovery allowed scenario 2 to act as carbon sink (-0.033 kgCO2eq center dot m-3). Therefore, coupling AnMBR, primary settling and anaerobic digestion improves the feasibility of sulfate-rich wastewater treatments compared to AnMBR alone. |
| publishDate |
2025 |
| dc.date.none.fl_str_mv |
2025 2025-04-01 2025 2025-04-08 2027 2027-02-28 |
| dc.type.none.fl_str_mv |
journal article http://purl.org/coar/resource_type/c_6501 VoR http://purl.org/coar/version/c_970fb48d4fbd8a85 |
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info:eu-repo/semantics/article |
| format |
article |
| dc.identifier.none.fl_str_mv |
https://riunet.upv.es/handle/10251/220370 |
| url |
https://riunet.upv.es/handle/10251/220370 |
| dc.language.none.fl_str_mv |
Inglés eng |
| language_invalid_str_mv |
Inglés |
| language |
eng |
| dc.relation.none.fl_str_mv |
Agencia Estatal de Investigación http://dx.doi.org/10.13039/501100011033 Plan Estatal de Investigación Científica y Técnica y de Innovación 2017-2020 PID2020-114315RB-C22 ESTUDIO DE TECNOLOGIAS PARA LA RECUPERACION DE NUTRIENTES DE LAS CORRIENTES OBTENIDAS EN INSTALACIONES DE RECUPERACION DE RECURSOS CON CARBONIZACION HIDROTERMAL DE LODOS. Ministerio de Economía y Competitividad http://dx.doi.org/10.13039/501100003329 BES-2015-073403 BES-2015-073403 Ministerio de Economía y Competitividad http://dx.doi.org/10.13039/501100003329 CTM2014-54980-C2-1-R OBTENCION DE BIONUTRIENTES Y ENERGIA DEL AGUA RESIDUAL URBANA MEDIANTE CULTIVO DE MICROALGAS, TRATAMIENTOS ANAEROBIOS, CRISTALIZACION DE FOSFORO, ABSORCION DE NH3 Y COMPOSTAJE |
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embargoed access http://purl.org/coar/access_right/c_f1cf Reconocimiento - No comercial - Sin obra derivada (by-nc-nd) http://creativecommons.org/licenses/by-nc-nd/4.0/ |
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info:eu-repo/semantics/embargoedAccess |
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embargoed access http://purl.org/coar/access_right/c_f1cf Reconocimiento - No comercial - Sin obra derivada (by-nc-nd) http://creativecommons.org/licenses/by-nc-nd/4.0/ |
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Elsevier |
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Elsevier |
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