Otimização das condições operacionais do sistema de tratamento biológico da água residuária proveniente da produção de fécula de mandioca

Detalhes bibliográficos
Autor(a) principal: Fleck, Leandro
Data de Publicação: 2018
Tipo de documento: Tese
Idioma: por
Título da fonte: Biblioteca Digital de Teses e Dissertações do UNIOESTE
Texto Completo: http://tede.unioeste.br/handle/tede/3723
Resumo: As a direct consequence of industrial development, the generation of organic waste exceeds the levels of the natural capacity for biological degradation. In the field of food production, the cassava starch stands out, because the wastewater coming from the processing of cassava, when not properly treated, results in a deterioration of the ecological balance. The present study aimed to optimize the main operating conditions that directly influence the efficiency of the processes of anaerobic biodigestion, nitrification and denitrification of the wastewater coming from cassava processing. For the anaerobic biodigestion process, an anaerobic reactor of 20 L, operating in a batch system was used. The effects of temperature and total volatile solids from the inoculum (TVSi) on the removal of chemical oxygen demand (COD) and total volatile solids of the reactor (TVSr) were evaluated using a Central Composite Rotational Design (CCRD), being the variables responses simultaneously evaluated by the desirability function. The effluent from the anaerobic biodigestion process was used as affluent for the nitrification of the wastewater. In this stage, an aerated reactor was used, with a useful volume of 4 L and aeration control by rotameter. The air flow and cycle time parameters were controlled, and their effects on the removal of ammoniacal nitrogen and conversion to nitrate were evaluated using a CCRD. The wastewater previously treated under anaerobic and aerobic optimized conditions was used as affluent for the denitrification process, performed under anoxic conditions in a reactor with a useful volume of 2 L, operating in a batch system. The temperature and COD:N ratio were monitored, and their effects on nitrite and nitrate removal were evaluated using a CCRD, with ethanol as the external carbon source. Simultaneous optimization of the response variables were performed using the desirability function technique. For the anaerobic treatment of wastewater, the highest COD removal (96.82%) occurred at 42 °C and 12.0% TVSi. The highest TVSr removal (69.31%) was recorded at 45 °C and 10.0% TVSi. The representative equations of the process are statistically significant at a confidence interval of the 90%. Based on the desirability function, it is observed that the optimum operating condition for the anaerobic reactor is 39.7 °C and 10.8% TVSi. The COD and TVSr removal efficiencies estimated under these operating conditions were 90.45 and 63.12%, respectively. In aerobic conditions, the highest ammoniacal nitrogen removal, of 96.62%, occurred under 24 hours conditions and 0.15 L min-1 Lreactor-1, and the lowest removal, of 24.48%, occurred under conditions of 7,08 hours and 0.15 L min-1 Lreactor-1. The highest conversion to nitrate, of 24.81%, occurred under conditions of 40.92 hours and 0.15 L min-1 Lreactor-1, and the lowest conversion, of 11.65%, occurred under the conditions 7.08 hours and 0.15 L min-1 Lreactor-1. The optimum operating values of the aerated reactor, obtained by the desirability function, are 29.25 hours and 0.22 L min-1 Lreactor-1. The efficiencies of ammoniacal nitrogen removal and conversion to nitrate estimated under these operating conditions were 94.66 and 23.49%, respectively. In anoxic conditions, the highest removals of nitrite and nitrate, 97.38 and 98.70%, occurred under the conditions of 22.50 °C and COD:N ratios of 5.00 and 8.00, respectively. The mathematical models representative of the process are statistically significant for the removal of nitrite and nitrate. The optimum values of temperature and COD:N ratio which result in higher efficiencies of nitrite and nitrate removals, simultaneously, are 24.32 ° C and 5.81, respectively. The nitrite and nitrate removal efficiencies estimated under these operating conditions were 97.46 and 98.70%, respectively. The optimization of the biological treatment of the starch wastewater, considering the interdependence between the steps, proved to be feasible and with satisfactory removal of the different constituents of interest for the process.
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spelling Tavares, Maria Herminia Ferreirahttp://lattes.cnpq.br/4169267827878056Tavares, Maria Herminia Ferreirahttp://lattes.cnpq.br/4169267827878056Eyng, Eduardohttp://lattes.cnpq.br/1101075438495044Frare, Laercio Mantovanihttp://lattes.cnpq.br/7676033878331606Gomes, Simone Damascenohttp://lattes.cnpq.br/3362104483832351Christ, Divairhttp://lattes.cnpq.br/6200553304840204http://lattes.cnpq.br/2381929054098695Fleck, Leandro2018-06-04T14:55:24Z2018-02-01FLECK, Leandro. Otimização das condições operacionais do sistema de tratamento biológico da água residuária proveniente da produção de fécula de mandioca. 2018. 102 f. Tese ( Doutorado em Engenharia Agrícola) - Universidade Estadual do Oeste do Paraná, Cascavel, 2018.http://tede.unioeste.br/handle/tede/3723As a direct consequence of industrial development, the generation of organic waste exceeds the levels of the natural capacity for biological degradation. In the field of food production, the cassava starch stands out, because the wastewater coming from the processing of cassava, when not properly treated, results in a deterioration of the ecological balance. The present study aimed to optimize the main operating conditions that directly influence the efficiency of the processes of anaerobic biodigestion, nitrification and denitrification of the wastewater coming from cassava processing. For the anaerobic biodigestion process, an anaerobic reactor of 20 L, operating in a batch system was used. The effects of temperature and total volatile solids from the inoculum (TVSi) on the removal of chemical oxygen demand (COD) and total volatile solids of the reactor (TVSr) were evaluated using a Central Composite Rotational Design (CCRD), being the variables responses simultaneously evaluated by the desirability function. The effluent from the anaerobic biodigestion process was used as affluent for the nitrification of the wastewater. In this stage, an aerated reactor was used, with a useful volume of 4 L and aeration control by rotameter. The air flow and cycle time parameters were controlled, and their effects on the removal of ammoniacal nitrogen and conversion to nitrate were evaluated using a CCRD. The wastewater previously treated under anaerobic and aerobic optimized conditions was used as affluent for the denitrification process, performed under anoxic conditions in a reactor with a useful volume of 2 L, operating in a batch system. The temperature and COD:N ratio were monitored, and their effects on nitrite and nitrate removal were evaluated using a CCRD, with ethanol as the external carbon source. Simultaneous optimization of the response variables were performed using the desirability function technique. For the anaerobic treatment of wastewater, the highest COD removal (96.82%) occurred at 42 °C and 12.0% TVSi. The highest TVSr removal (69.31%) was recorded at 45 °C and 10.0% TVSi. The representative equations of the process are statistically significant at a confidence interval of the 90%. Based on the desirability function, it is observed that the optimum operating condition for the anaerobic reactor is 39.7 °C and 10.8% TVSi. The COD and TVSr removal efficiencies estimated under these operating conditions were 90.45 and 63.12%, respectively. In aerobic conditions, the highest ammoniacal nitrogen removal, of 96.62%, occurred under 24 hours conditions and 0.15 L min-1 Lreactor-1, and the lowest removal, of 24.48%, occurred under conditions of 7,08 hours and 0.15 L min-1 Lreactor-1. The highest conversion to nitrate, of 24.81%, occurred under conditions of 40.92 hours and 0.15 L min-1 Lreactor-1, and the lowest conversion, of 11.65%, occurred under the conditions 7.08 hours and 0.15 L min-1 Lreactor-1. The optimum operating values of the aerated reactor, obtained by the desirability function, are 29.25 hours and 0.22 L min-1 Lreactor-1. The efficiencies of ammoniacal nitrogen removal and conversion to nitrate estimated under these operating conditions were 94.66 and 23.49%, respectively. In anoxic conditions, the highest removals of nitrite and nitrate, 97.38 and 98.70%, occurred under the conditions of 22.50 °C and COD:N ratios of 5.00 and 8.00, respectively. The mathematical models representative of the process are statistically significant for the removal of nitrite and nitrate. The optimum values of temperature and COD:N ratio which result in higher efficiencies of nitrite and nitrate removals, simultaneously, are 24.32 ° C and 5.81, respectively. The nitrite and nitrate removal efficiencies estimated under these operating conditions were 97.46 and 98.70%, respectively. The optimization of the biological treatment of the starch wastewater, considering the interdependence between the steps, proved to be feasible and with satisfactory removal of the different constituents of interest for the process.Como consequência direta do desenvolvimento industrial, a geração de resíduos orgânicos supera os níveis da capacidade natural de degradação biológica. No âmbito da produção de alimentos, as fecularias de mandioca se destacam, pois a água residuária proveniente do processamento da mandioca, quando não adequadamente tratada, resulta na deterioração do equilíbrio ecológico. O presente estudo teve como objetivo otimizar as principais condições operacionais que influenciam na eficiência dos processos de biodigestão anaeróbia, nitrificação e desnitrificação da água residuária proveniente do processamento da mandioca. Para o processo de biodigestão anaeróbia utilizou-se um reator de 20 L, operando em sistema de batelada. Foram avaliados os efeitos da temperatura e dos sólidos totais voláteis do inóculo (STVi) sobre a remoção da demanda química de oxigênio (DQO) e sólidos totais voláteis do reator (STVr), utilizando um Delineamento Composto Central Rotacional (DCCR), sendo as variáveis respostas avaliadas simultaneamente pela função de desejabilidade. O efluente proveniente do processo de biodigestão anaeróbia foi utilizado como afluente para a nitrificação da água residuária. Nesta etapa utilizou-se um reator aerado, com volume útil de 4 L e controle de aeração por rotâmetro. Foram controlados os parâmetros fluxo de ar e tempo de ciclo, avaliando-se seus efeitos sobre a remoção de nitrogênio amoniacal e a conversão a nitrato, utilizando-se um DCCR. A água residuária previamente tratada em condições anaeróbias e aeróbias otimizadas foi utilizada como afluente para o processo de desnitrificação, realizado em condições anóxicas em um reator com volume útil de 2 L, operando em sistema de batelada. Foram controlados os parâmetros temperatura e relação DQO:N, sendo seus efeitos sobre a remoção de nitrito e nitrato avaliados utilizando-se um DCCR, com etanol como fonte externa de carbono. A otimização simultânea das variáveis-respostas foi realizada utilizando a técnica da função de desejabilidade. Para o tratamento anaeróbio da água residuária a remoção mais elevada de DQO (96,82%) ocorreu a 42 °C e 12,0% de STVi. A maior remoção de STVr (69,31%) foi registrada a 45 °C e 10,0% de STVi. As equações representativas do processo são estatisticamente significativas a um intervalo de confiança de 90%. Com base na função de desejabilidade, observa-se que a condição operacional ótima para o reator anaeróbio é de 39,7 °C e 10,8% de STVi. As eficiências de remoção de DQO e STVr estimadas nestas condições operacionais foram de 90,45 e 63,12%, respectivamente. Em condições aeróbias, a maior remoção de nitrogênio amoniacal, de 96,62%, ocorreu nas condições de 24 horas e 0,15 L min-1 Lreator-1, e a menor remoção, de 24,48%, ocorreu nas condições 7,08 horas e 0,15 L min-1 Lreator-1. A maior conversão a nitrato, de 24,81%, ocorreu nas condições de 40,92 horas e 0,15 L min-1 Lreator-1, e a menor conversão, de 11,65%, ocorreu nas condições 7,08 horas e 0,15 L min-1 Lreator-1. Os valores ótimos de operação do reator aerado, obtidos pela função de desejabilidade, são de 29,25 horas e 0,22 L min-1 Lreator-1. As eficiências de remoção de nitrogênio amoniacal e conversão a nitrato estimadas nestas condições operacionais foram de 94,66 e 23,49%, respectivamente. Em condições anóxicas as maiores remoções de nitrito e nitrato, de 97,38 e 98,70%, ocorreram nas condições de 22,50 °C e relações DQO:N de 5,00 e 8,00, respectivamente. Os modelos matemáticos representativos do processo são estatisticamente significativos para remoção de nitrito e nitrato. Os valores ótimos de temperatura e relação DQO:N que resultam em maiores eficiências de remoções de nitrito e nitrato, simultaneamente, são de 24,32 °C e 5,81, respectivamente. As eficiências de remoção de nitrito e nitrato estimadas nestas condições operacionais foram de 97,46 e 98,70%, respectivamente. A otimização do tratamento biológico do efluente de fecularia, considerando a interdependência entre as etapas, mostrou-se viável e com remoção satisfatória dos diferentes constituintes de interesse para o processo.Submitted by Rosangela Silva (rosangela.silva3@unioeste.br) on 2018-06-04T14:55:24Z No. of bitstreams: 2 Leandro Fleck.pdf: 1468286 bytes, checksum: 89cca0c76a9f2e0200eb49ec5186fb83 (MD5) license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5)Made available in DSpace on 2018-06-04T14:55:24Z (GMT). No. of bitstreams: 2 Leandro Fleck.pdf: 1468286 bytes, checksum: 89cca0c76a9f2e0200eb49ec5186fb83 (MD5) license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) Previous issue date: 2018-02-01Coordenação de Aperfeiçoamento de Pessoal de Nível Superior - CAPESapplication/pdfpor6588633818200016417500Universidade Estadual do Oeste do ParanáCascavelPrograma de Pós-Graduação em Engenharia AgrícolaUNIOESTEBrasilCentro de Ciências Exatas e Tecnológicashttp://creativecommons.org/licenses/by-nc-nd/4.0/info:eu-repo/semantics/openAccessDigestão anaeróbiaBiogásDesnitrificaçãoModelos matemáticosNitrificaçãoNutrientesAnaerobic digestionDenitrificationMathematical modelsNitrificationNutrientsCIENCIAS EXATAS E DA TERRAOtimização das condições operacionais do sistema de tratamento biológico da água residuária proveniente da produção de fécula de mandiocaOptimization of the operational conditions of the system biological treatment of wastewater from cassava starch productioninfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/doctoralThesis-53476924504160521296006006006002214374442868382015-45373260596047840162075167498588264571reponame:Biblioteca Digital de Teses e Dissertações do UNIOESTEinstname:Universidade Estadual do Oeste do Paraná (UNIOESTE)instacron:UNIOESTEORIGINALLeandro Fleck.pdfLeandro Fleck.pdfapplication/pdf1468286http://tede.unioeste.br:8080/tede/bitstream/tede/3723/5/Leandro+Fleck.pdf89cca0c76a9f2e0200eb49ec5186fb83MD55CC-LICENSElicense_urllicense_urltext/plain; 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dc.title.por.fl_str_mv Otimização das condições operacionais do sistema de tratamento biológico da água residuária proveniente da produção de fécula de mandioca
dc.title.alternative.eng.fl_str_mv Optimization of the operational conditions of the system biological treatment of wastewater from cassava starch production
title Otimização das condições operacionais do sistema de tratamento biológico da água residuária proveniente da produção de fécula de mandioca
spellingShingle Otimização das condições operacionais do sistema de tratamento biológico da água residuária proveniente da produção de fécula de mandioca
Fleck, Leandro
Digestão anaeróbia
Biogás
Desnitrificação
Modelos matemáticos
Nitrificação
Nutrientes
Anaerobic digestion
Denitrification
Mathematical models
Nitrification
Nutrients
CIENCIAS EXATAS E DA TERRA
title_short Otimização das condições operacionais do sistema de tratamento biológico da água residuária proveniente da produção de fécula de mandioca
title_full Otimização das condições operacionais do sistema de tratamento biológico da água residuária proveniente da produção de fécula de mandioca
title_fullStr Otimização das condições operacionais do sistema de tratamento biológico da água residuária proveniente da produção de fécula de mandioca
title_full_unstemmed Otimização das condições operacionais do sistema de tratamento biológico da água residuária proveniente da produção de fécula de mandioca
title_sort Otimização das condições operacionais do sistema de tratamento biológico da água residuária proveniente da produção de fécula de mandioca
author Fleck, Leandro
author_facet Fleck, Leandro
author_role author
dc.contributor.advisor1.fl_str_mv Tavares, Maria Herminia Ferreira
dc.contributor.advisor1Lattes.fl_str_mv http://lattes.cnpq.br/4169267827878056
dc.contributor.referee1.fl_str_mv Tavares, Maria Herminia Ferreira
dc.contributor.referee1Lattes.fl_str_mv http://lattes.cnpq.br/4169267827878056
dc.contributor.referee2.fl_str_mv Eyng, Eduardo
dc.contributor.referee2Lattes.fl_str_mv http://lattes.cnpq.br/1101075438495044
dc.contributor.referee3.fl_str_mv Frare, Laercio Mantovani
dc.contributor.referee3Lattes.fl_str_mv http://lattes.cnpq.br/7676033878331606
dc.contributor.referee4.fl_str_mv Gomes, Simone Damasceno
dc.contributor.referee4Lattes.fl_str_mv http://lattes.cnpq.br/3362104483832351
dc.contributor.referee5.fl_str_mv Christ, Divair
dc.contributor.referee5Lattes.fl_str_mv http://lattes.cnpq.br/6200553304840204
dc.contributor.authorLattes.fl_str_mv http://lattes.cnpq.br/2381929054098695
dc.contributor.author.fl_str_mv Fleck, Leandro
contributor_str_mv Tavares, Maria Herminia Ferreira
Tavares, Maria Herminia Ferreira
Eyng, Eduardo
Frare, Laercio Mantovani
Gomes, Simone Damasceno
Christ, Divair
dc.subject.por.fl_str_mv Digestão anaeróbia
Biogás
Desnitrificação
Modelos matemáticos
Nitrificação
Nutrientes
topic Digestão anaeróbia
Biogás
Desnitrificação
Modelos matemáticos
Nitrificação
Nutrientes
Anaerobic digestion
Denitrification
Mathematical models
Nitrification
Nutrients
CIENCIAS EXATAS E DA TERRA
dc.subject.eng.fl_str_mv Anaerobic digestion
Denitrification
Mathematical models
Nitrification
Nutrients
dc.subject.cnpq.fl_str_mv CIENCIAS EXATAS E DA TERRA
description As a direct consequence of industrial development, the generation of organic waste exceeds the levels of the natural capacity for biological degradation. In the field of food production, the cassava starch stands out, because the wastewater coming from the processing of cassava, when not properly treated, results in a deterioration of the ecological balance. The present study aimed to optimize the main operating conditions that directly influence the efficiency of the processes of anaerobic biodigestion, nitrification and denitrification of the wastewater coming from cassava processing. For the anaerobic biodigestion process, an anaerobic reactor of 20 L, operating in a batch system was used. The effects of temperature and total volatile solids from the inoculum (TVSi) on the removal of chemical oxygen demand (COD) and total volatile solids of the reactor (TVSr) were evaluated using a Central Composite Rotational Design (CCRD), being the variables responses simultaneously evaluated by the desirability function. The effluent from the anaerobic biodigestion process was used as affluent for the nitrification of the wastewater. In this stage, an aerated reactor was used, with a useful volume of 4 L and aeration control by rotameter. The air flow and cycle time parameters were controlled, and their effects on the removal of ammoniacal nitrogen and conversion to nitrate were evaluated using a CCRD. The wastewater previously treated under anaerobic and aerobic optimized conditions was used as affluent for the denitrification process, performed under anoxic conditions in a reactor with a useful volume of 2 L, operating in a batch system. The temperature and COD:N ratio were monitored, and their effects on nitrite and nitrate removal were evaluated using a CCRD, with ethanol as the external carbon source. Simultaneous optimization of the response variables were performed using the desirability function technique. For the anaerobic treatment of wastewater, the highest COD removal (96.82%) occurred at 42 °C and 12.0% TVSi. The highest TVSr removal (69.31%) was recorded at 45 °C and 10.0% TVSi. The representative equations of the process are statistically significant at a confidence interval of the 90%. Based on the desirability function, it is observed that the optimum operating condition for the anaerobic reactor is 39.7 °C and 10.8% TVSi. The COD and TVSr removal efficiencies estimated under these operating conditions were 90.45 and 63.12%, respectively. In aerobic conditions, the highest ammoniacal nitrogen removal, of 96.62%, occurred under 24 hours conditions and 0.15 L min-1 Lreactor-1, and the lowest removal, of 24.48%, occurred under conditions of 7,08 hours and 0.15 L min-1 Lreactor-1. The highest conversion to nitrate, of 24.81%, occurred under conditions of 40.92 hours and 0.15 L min-1 Lreactor-1, and the lowest conversion, of 11.65%, occurred under the conditions 7.08 hours and 0.15 L min-1 Lreactor-1. The optimum operating values of the aerated reactor, obtained by the desirability function, are 29.25 hours and 0.22 L min-1 Lreactor-1. The efficiencies of ammoniacal nitrogen removal and conversion to nitrate estimated under these operating conditions were 94.66 and 23.49%, respectively. In anoxic conditions, the highest removals of nitrite and nitrate, 97.38 and 98.70%, occurred under the conditions of 22.50 °C and COD:N ratios of 5.00 and 8.00, respectively. The mathematical models representative of the process are statistically significant for the removal of nitrite and nitrate. The optimum values of temperature and COD:N ratio which result in higher efficiencies of nitrite and nitrate removals, simultaneously, are 24.32 ° C and 5.81, respectively. The nitrite and nitrate removal efficiencies estimated under these operating conditions were 97.46 and 98.70%, respectively. The optimization of the biological treatment of the starch wastewater, considering the interdependence between the steps, proved to be feasible and with satisfactory removal of the different constituents of interest for the process.
publishDate 2018
dc.date.accessioned.fl_str_mv 2018-06-04T14:55:24Z
dc.date.issued.fl_str_mv 2018-02-01
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/doctoralThesis
format doctoralThesis
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dc.identifier.citation.fl_str_mv FLECK, Leandro. Otimização das condições operacionais do sistema de tratamento biológico da água residuária proveniente da produção de fécula de mandioca. 2018. 102 f. Tese ( Doutorado em Engenharia Agrícola) - Universidade Estadual do Oeste do Paraná, Cascavel, 2018.
dc.identifier.uri.fl_str_mv http://tede.unioeste.br/handle/tede/3723
identifier_str_mv FLECK, Leandro. Otimização das condições operacionais do sistema de tratamento biológico da água residuária proveniente da produção de fécula de mandioca. 2018. 102 f. Tese ( Doutorado em Engenharia Agrícola) - Universidade Estadual do Oeste do Paraná, Cascavel, 2018.
url http://tede.unioeste.br/handle/tede/3723
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language por
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dc.relation.department.fl_str_mv 2214374442868382015
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dc.relation.sponsorship.fl_str_mv 2075167498588264571
dc.rights.driver.fl_str_mv http://creativecommons.org/licenses/by-nc-nd/4.0/
info:eu-repo/semantics/openAccess
rights_invalid_str_mv http://creativecommons.org/licenses/by-nc-nd/4.0/
eu_rights_str_mv openAccess
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dc.publisher.none.fl_str_mv Universidade Estadual do Oeste do Paraná
Cascavel
dc.publisher.program.fl_str_mv Programa de Pós-Graduação em Engenharia Agrícola
dc.publisher.initials.fl_str_mv UNIOESTE
dc.publisher.country.fl_str_mv Brasil
dc.publisher.department.fl_str_mv Centro de Ciências Exatas e Tecnológicas
publisher.none.fl_str_mv Universidade Estadual do Oeste do Paraná
Cascavel
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