Anaerobic Nitrogen Removal: The start-up of an Anammox Reactor with pre-treated Real wastewater from the Anaerobic Digestion of municipal solid waste

Detalhes bibliográficos
Autor(a) principal: Bernardo, Tiago Emanuel do Espírito Santo
Data de Publicação: 2017
Tipo de documento: Dissertação
Idioma: eng
Título da fonte: Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
Texto Completo: http://hdl.handle.net/10362/29115
Resumo: In this study, wastewater produced by the Anaerobic Digestion of municipal solid waste and pre-treated by partial-nitrification was fed to a granular Anammox reactor. A conservative exponential Law was used to slowly replace the synthetic wastewater for the pre-treated wastewater, starting at 10%. This strategy was adopted in order to avoid stressful conditions to bacteria, which could thus acclimate to the reactor conditions. The experiment was divided in two phases, the first one with increasing real wastewater ratio and a second phase totally fed with real wastewater. The influent is characterized by a nitrogen loading rate of 1.5gNL-1d-1, with a NO2-N/NH4-N ratio of 1.20. Removal efficiencies were stable during all experiment, around 90%. The Anammox activity also increased during the experimentation. The Volatile suspended solids grown during phase 1 of experiment, with an initial value of 4,2 gVSSL-1. The kinetics assay results also helped checking out the removal rates for ammonium and nitrite, and production rates for nitrate. On the average the specific nitrate and ammonium removal rate, with continues NLR was 0,370,07 g NO2-N gVSS-1d-1 and 0,270,07 gNH4-N/gVSS-1d-1, respectively. For nitrate production was 0,0550,030 gNO3-NgVSS-1d-1, The organic carbon removal was also tested. The effluent values were variable, and real wastewater had no direct effect on the capability of the Anammox process to remove organic carbon. This is due to a perfect partial-nitrification, who allowed the real effluent to have low organic carbon, which not developed inhibition effect to the Anammox bacteria. During phase 2, the reactor was fed with real wastewater without any pre-treatment. This experiment wasn’t very successful, and Anammox system failed. After, was again fed with synthetic wastewater and the bacteria could recover. Results showed that the process can work with this type of wastewater, if a conservative start-up strategy is adopted and a partial-nitrification step is used to remove organic carbon.
id RCAP_63d623eb9335b2050bb6139988c932dc
oai_identifier_str oai:run.unl.pt:10362/29115
network_acronym_str RCAP
network_name_str Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
repository_id_str
spelling Anaerobic Nitrogen Removal: The start-up of an Anammox Reactor with pre-treated Real wastewater from the Anaerobic Digestion of municipal solid wasteAnaerobic digestionAnammoxpartial-nitrificationammoniumnitritereal wastewaterDomínio/Área Científica::Engenharia e Tecnologia::Engenharia QuímicaIn this study, wastewater produced by the Anaerobic Digestion of municipal solid waste and pre-treated by partial-nitrification was fed to a granular Anammox reactor. A conservative exponential Law was used to slowly replace the synthetic wastewater for the pre-treated wastewater, starting at 10%. This strategy was adopted in order to avoid stressful conditions to bacteria, which could thus acclimate to the reactor conditions. The experiment was divided in two phases, the first one with increasing real wastewater ratio and a second phase totally fed with real wastewater. The influent is characterized by a nitrogen loading rate of 1.5gNL-1d-1, with a NO2-N/NH4-N ratio of 1.20. Removal efficiencies were stable during all experiment, around 90%. The Anammox activity also increased during the experimentation. The Volatile suspended solids grown during phase 1 of experiment, with an initial value of 4,2 gVSSL-1. The kinetics assay results also helped checking out the removal rates for ammonium and nitrite, and production rates for nitrate. On the average the specific nitrate and ammonium removal rate, with continues NLR was 0,370,07 g NO2-N gVSS-1d-1 and 0,270,07 gNH4-N/gVSS-1d-1, respectively. For nitrate production was 0,0550,030 gNO3-NgVSS-1d-1, The organic carbon removal was also tested. The effluent values were variable, and real wastewater had no direct effect on the capability of the Anammox process to remove organic carbon. This is due to a perfect partial-nitrification, who allowed the real effluent to have low organic carbon, which not developed inhibition effect to the Anammox bacteria. During phase 2, the reactor was fed with real wastewater without any pre-treatment. This experiment wasn’t very successful, and Anammox system failed. After, was again fed with synthetic wastewater and the bacteria could recover. Results showed that the process can work with this type of wastewater, if a conservative start-up strategy is adopted and a partial-nitrification step is used to remove organic carbon.Carucci, AlessandraMilia, StefanoRUNBernardo, Tiago Emanuel do Espírito Santo2018-01-26T12:49:06Z2017-1120172017-11-01T00:00:00Zinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/masterThesisapplication/pdfhttp://hdl.handle.net/10362/29115enginfo:eu-repo/semantics/openAccessreponame:Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)instname:Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informaçãoinstacron:RCAAP2023-07-10T15:42:08ZPortal AgregadorONG
dc.title.none.fl_str_mv Anaerobic Nitrogen Removal: The start-up of an Anammox Reactor with pre-treated Real wastewater from the Anaerobic Digestion of municipal solid waste
title Anaerobic Nitrogen Removal: The start-up of an Anammox Reactor with pre-treated Real wastewater from the Anaerobic Digestion of municipal solid waste
spellingShingle Anaerobic Nitrogen Removal: The start-up of an Anammox Reactor with pre-treated Real wastewater from the Anaerobic Digestion of municipal solid waste
Bernardo, Tiago Emanuel do Espírito Santo
Anaerobic digestion
Anammox
partial-nitrification
ammonium
nitrite
real wastewater
Domínio/Área Científica::Engenharia e Tecnologia::Engenharia Química
title_short Anaerobic Nitrogen Removal: The start-up of an Anammox Reactor with pre-treated Real wastewater from the Anaerobic Digestion of municipal solid waste
title_full Anaerobic Nitrogen Removal: The start-up of an Anammox Reactor with pre-treated Real wastewater from the Anaerobic Digestion of municipal solid waste
title_fullStr Anaerobic Nitrogen Removal: The start-up of an Anammox Reactor with pre-treated Real wastewater from the Anaerobic Digestion of municipal solid waste
title_full_unstemmed Anaerobic Nitrogen Removal: The start-up of an Anammox Reactor with pre-treated Real wastewater from the Anaerobic Digestion of municipal solid waste
title_sort Anaerobic Nitrogen Removal: The start-up of an Anammox Reactor with pre-treated Real wastewater from the Anaerobic Digestion of municipal solid waste
author Bernardo, Tiago Emanuel do Espírito Santo
author_facet Bernardo, Tiago Emanuel do Espírito Santo
author_role author
dc.contributor.none.fl_str_mv Carucci, Alessandra
Milia, Stefano
RUN
dc.contributor.author.fl_str_mv Bernardo, Tiago Emanuel do Espírito Santo
dc.subject.por.fl_str_mv Anaerobic digestion
Anammox
partial-nitrification
ammonium
nitrite
real wastewater
Domínio/Área Científica::Engenharia e Tecnologia::Engenharia Química
topic Anaerobic digestion
Anammox
partial-nitrification
ammonium
nitrite
real wastewater
Domínio/Área Científica::Engenharia e Tecnologia::Engenharia Química
description In this study, wastewater produced by the Anaerobic Digestion of municipal solid waste and pre-treated by partial-nitrification was fed to a granular Anammox reactor. A conservative exponential Law was used to slowly replace the synthetic wastewater for the pre-treated wastewater, starting at 10%. This strategy was adopted in order to avoid stressful conditions to bacteria, which could thus acclimate to the reactor conditions. The experiment was divided in two phases, the first one with increasing real wastewater ratio and a second phase totally fed with real wastewater. The influent is characterized by a nitrogen loading rate of 1.5gNL-1d-1, with a NO2-N/NH4-N ratio of 1.20. Removal efficiencies were stable during all experiment, around 90%. The Anammox activity also increased during the experimentation. The Volatile suspended solids grown during phase 1 of experiment, with an initial value of 4,2 gVSSL-1. The kinetics assay results also helped checking out the removal rates for ammonium and nitrite, and production rates for nitrate. On the average the specific nitrate and ammonium removal rate, with continues NLR was 0,370,07 g NO2-N gVSS-1d-1 and 0,270,07 gNH4-N/gVSS-1d-1, respectively. For nitrate production was 0,0550,030 gNO3-NgVSS-1d-1, The organic carbon removal was also tested. The effluent values were variable, and real wastewater had no direct effect on the capability of the Anammox process to remove organic carbon. This is due to a perfect partial-nitrification, who allowed the real effluent to have low organic carbon, which not developed inhibition effect to the Anammox bacteria. During phase 2, the reactor was fed with real wastewater without any pre-treatment. This experiment wasn’t very successful, and Anammox system failed. After, was again fed with synthetic wastewater and the bacteria could recover. Results showed that the process can work with this type of wastewater, if a conservative start-up strategy is adopted and a partial-nitrification step is used to remove organic carbon.
publishDate 2017
dc.date.none.fl_str_mv 2017-11
2017
2017-11-01T00:00:00Z
2018-01-26T12:49:06Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/masterThesis
format masterThesis
status_str publishedVersion
dc.identifier.uri.fl_str_mv http://hdl.handle.net/10362/29115
url http://hdl.handle.net/10362/29115
dc.language.iso.fl_str_mv eng
language eng
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv application/pdf
dc.source.none.fl_str_mv reponame:Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
instname:Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação
instacron:RCAAP
instname_str Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação
instacron_str RCAAP
institution RCAAP
reponame_str Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
collection Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
repository.name.fl_str_mv
repository.mail.fl_str_mv
_version_ 1777302956867059712