Produção de hidrogênio e metabólitos em reator anaeróbio de leito fluidizado e em reator de leito granular expandido a partir de glicerol

Detalhes bibliográficos
Ano de defesa: 2014
Autor(a) principal: Bosio, Morgana
Orientador(a): Silva, Edson Luiz lattes
Banca de defesa: Não Informado pela instituição
Tipo de documento: Dissertação
Tipo de acesso: Acesso aberto
Idioma: por
Instituição de defesa: Universidade Federal de São Carlos
Câmpus São Carlos
Programa de Pós-Graduação: Programa de Pós-Graduação em Engenharia Química - PPGEQ
Departamento: Não Informado pela instituição
País: Não Informado pela instituição
Palavras-chave em Português:
TDH
Palavras-chave em Inglês:
HRT
Área do conhecimento CNPq:
Link de acesso: https://repositorio.ufscar.br/handle/ufscar/7361
Resumo: This work aimed to evaluated the biological hydrogen production using crude glycerol as feedstock in two anaerobic reactors: (1) anaerobic fluidized bed reactor (AFBR), that allows high mass transfer, and (2) an expanded granular sludge blanket reactor, that can used with high efficiency even at high organic loading. In the AFBR, it was evaluated the influence of HRT (14, 12, 10, 8, 6, 4, 2 and 1 hour) in the hydrogen production using crude glycerol as feedstock at 5 g.L-1 and expanded clay as support material. In the EGSB, the HRT varied from 24 to 1 hour, it was used the same feedstock as that used in the AFBR. The reactors were maintained at controlled temperature at 30°C. The noculum for AFBR and EGSB was granular sludge taken from UASB reactor treating poultry slaughterhouse that was previously submitted to heat treatment. In the AFBR, the hydrogen production rate (HPR) increased from 0.08 to 0.73L.h-1.L -1 with the decrease at HRT from 14 to 1 hour, respectively. The hydrogen yield (HY) did not presented the same trend and remained almost unchanged (0.62, 0.76, 0.73, 0.75, 0.60, 0.58, 0.69, 0.85 molH2.mol-1glycerol). For this reactor, the main byproducts were 1,3-propanediol (1,3-PD), ethanol, acetic, butyric and propionic acid. The highest 1,3-PD (1,230 mg.L-1), ethanol (723 mg.L-1), acetic acid (204 mg.L-1), propionic acid (759 mg.L-1) and butyric acid (324 mg.L-1) concentration occurred at HRT of 6, 14, 8, 2, 6 hours, respectively. In the EGSB, the HPR and the HY presented the same trend: HPR increased from 0.018 to 1.708 L.h-1.L-1 and HY increased from 0.19 to 2.87 molH2.mol-1glycerol with the decrease in the HRT from 14 to 1 hour. For both reactors, the AFBR and the EGSB,the highest HPR and HY occurred at HRT of 1 hour. As well as for the AFBR, the main byproducts quantified in the EGSB were 1,3-propanediol (1,3-PD), ethanol, acetic, butyric and propionic acid. The highest 1,3-PD (1,606 mg.L -1), ethanol (400 mg.L-1), acetic acid (219 mg.L-1), propionic acid (1,075 mg.L-1) and butyric acid (248 mg.L-1) concentration occurred at HRT of 16, 12, 16, 8, 20 hours, respectively.
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spelling Bosio, MorganaSilva, Edson Luizhttp://lattes.cnpq.br/9720274214573371http://lattes.cnpq.br/66399563308960502016-09-21T18:32:00Z2016-09-21T18:32:00Z2014-03-28BOSIO, Morgana. Produção de hidrogênio e metabólitos em reator anaeróbio de leito fluidizado e em reator de leito granular expandido a partir de glicerol. 2014. Dissertação (Mestrado em Engenharia Química) – Universidade Federal de São Carlos, São Carlos, 2014. Disponível em: https://repositorio.ufscar.br/handle/ufscar/7361.https://repositorio.ufscar.br/handle/ufscar/7361This work aimed to evaluated the biological hydrogen production using crude glycerol as feedstock in two anaerobic reactors: (1) anaerobic fluidized bed reactor (AFBR), that allows high mass transfer, and (2) an expanded granular sludge blanket reactor, that can used with high efficiency even at high organic loading. In the AFBR, it was evaluated the influence of HRT (14, 12, 10, 8, 6, 4, 2 and 1 hour) in the hydrogen production using crude glycerol as feedstock at 5 g.L-1 and expanded clay as support material. In the EGSB, the HRT varied from 24 to 1 hour, it was used the same feedstock as that used in the AFBR. The reactors were maintained at controlled temperature at 30°C. The noculum for AFBR and EGSB was granular sludge taken from UASB reactor treating poultry slaughterhouse that was previously submitted to heat treatment. In the AFBR, the hydrogen production rate (HPR) increased from 0.08 to 0.73L.h-1.L -1 with the decrease at HRT from 14 to 1 hour, respectively. The hydrogen yield (HY) did not presented the same trend and remained almost unchanged (0.62, 0.76, 0.73, 0.75, 0.60, 0.58, 0.69, 0.85 molH2.mol-1glycerol). For this reactor, the main byproducts were 1,3-propanediol (1,3-PD), ethanol, acetic, butyric and propionic acid. The highest 1,3-PD (1,230 mg.L-1), ethanol (723 mg.L-1), acetic acid (204 mg.L-1), propionic acid (759 mg.L-1) and butyric acid (324 mg.L-1) concentration occurred at HRT of 6, 14, 8, 2, 6 hours, respectively. In the EGSB, the HPR and the HY presented the same trend: HPR increased from 0.018 to 1.708 L.h-1.L-1 and HY increased from 0.19 to 2.87 molH2.mol-1glycerol with the decrease in the HRT from 14 to 1 hour. For both reactors, the AFBR and the EGSB,the highest HPR and HY occurred at HRT of 1 hour. As well as for the AFBR, the main byproducts quantified in the EGSB were 1,3-propanediol (1,3-PD), ethanol, acetic, butyric and propionic acid. The highest 1,3-PD (1,606 mg.L -1), ethanol (400 mg.L-1), acetic acid (219 mg.L-1), propionic acid (1,075 mg.L-1) and butyric acid (248 mg.L-1) concentration occurred at HRT of 16, 12, 16, 8, 20 hours, respectively.O presente estudo avaliou a produção biológica de hidrogênio utilizando glicerol bruto como matéria-prima em dois reatores anaeróbios: (1) reator anaeróbio de leito fluidizado (RALF), que possibilita elevada transferência de massa, e (2) um reator de leito granular expandido (EGSB), que pode apresentar alta eficiência mesmo quando aplicadas elevadas cargas orgânicas. No RALF, foi avaliada a influência do TDH (14, 12, 10, 8, 6, 4, 2 e 1 hora) na produção de hidrogênio utilizando o glicerol bruto como matéria-prima na concentração de 5 g.L-1 e argila expandida como material de suporte. No EGSB, o TDH estudado variou de 24 a 1 hora, e o substrato e a concentração foram as mesmas que os utilizadas no RALF. Os reatores foram mantidos em temperatura controlada de 30 °C. O inóculo para ambos os reatores, RALF e EGSB, foi lodo granular de reator UASB utilizado no tratamento de água residuária de abatedouro de aves, que foi previamente submetido ao tratamento térmico. No RALF, a taxa de produção de hidrogênio (HPR) aumentou de 0,08 para 0,73L.h-1.L- 1 com a diminuição do TDH de 14 para 1 hora, respectivamente. O rendimento de hidrogênio (HY) não apresentou a mesma tendência e manteve-se praticamente inalterado (0,62; 0,76; 0,73; 0,75; 0,60; 0,58; 0,69 e 0,85 molH2.mol-1glicerol) . Para este reator, os principais metabólitos foram 1,3-propanodiol (1,3-PD), etanol, ácido acético, butírico e propiônico. A maior concentração de 1,3- PD (1.230 mg.l-1), etanol (723 mg.L -1 ), ácido acético (204 mg.L-1), ácido propiônico (759 mg.L-1) e ácido butírico (324 mg.L-1) foi observada nos TDH de 6, 14, 8, 2, 6 horas, respectivamente. No EGSB, o HPR e HY apresentaram a mesma tendência: o HPR aumentou de 0,018-1,708 L.h-1.L-1 e o HY aumentou de 0,19-2,87 molH2.mol-1 glicerol com a diminuição do TDH de 14 para 1 hora. Para ambos os reatores, o RALF e o EGSB, a maior HPR e o maior HY foram observados no TDH de 1 hora. Assim como para o RALF, os principais metabólitos quantificados no EGSB foram 1,3- propanodiol (1,3-PD), etanol, ácido acético, ácido butírico e ácido propiônico. A maior concentração de 1,3- PD (1.606 mg.L-1), etanol (400 mg.L -1), ácido acético (219 mg.L-1), ácido propiônico (1.07 mg.L -1) e ácido butírico (248 mg.L -1) foi observada no TDH de 16, 12, 16, 8 e 20 horas, respectivamente.Não recebi financiamentoporUniversidade Federal de São CarlosCâmpus São CarlosPrograma de Pós-Graduação em Engenharia Química - PPGEQUFSCarTDHBiodieselTemperatura mesofílicaCultura mistaMetabólitosHRTBiodieselMesophilic temperatureMixed cultureByproductsENGENHARIAS::ENGENHARIA QUIMICAProdução de hidrogênio e metabólitos em reator anaeróbio de leito fluidizado e em reator de leito granular expandido a partir de glicerolinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/masterThesisOnlineinfo:eu-repo/semantics/openAccessreponame:Repositório Institucional da UFSCARinstname:Universidade Federal de São Carlos (UFSCAR)instacron:UFSCARORIGINALDissMB.pdfDissMB.pdfapplication/pdf3232973https://{{ getenv "DSPACE_HOST" "repositorio.ufscar.br" }}/bitstream/ufscar/7361/1/DissMB.pdf2ca9f79e6634a4d39d6cb45bd3047475MD51LICENSElicense.txtlicense.txttext/plain; charset=utf-81957https://{{ getenv "DSPACE_HOST" "repositorio.ufscar.br" }}/bitstream/ufscar/7361/2/license.txtae0398b6f8b235e40ad82cba6c50031dMD52TEXTDissMB.pdf.txtDissMB.pdf.txtExtracted texttext/plain197171https://{{ getenv "DSPACE_HOST" "repositorio.ufscar.br" }}/bitstream/ufscar/7361/3/DissMB.pdf.txte49c89f5302552059eee3b3033d3269dMD53THUMBNAILDissMB.pdf.jpgDissMB.pdf.jpgIM Thumbnailimage/jpeg6369https://{{ getenv "DSPACE_HOST" "repositorio.ufscar.br" }}/bitstream/ufscar/7361/4/DissMB.pdf.jpga8faae60f000d9e92c7f5870a2ea79f8MD54ufscar/73612019-09-11 02:10:52.267oai:repositorio.ufscar.br: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Repositório InstitucionalPUBhttps://repositorio.ufscar.br/oai/requestopendoar:43222023-05-25T12:52:18.123493Repositório Institucional da UFSCAR - Universidade Federal de São Carlos (UFSCAR)false
dc.title.por.fl_str_mv Produção de hidrogênio e metabólitos em reator anaeróbio de leito fluidizado e em reator de leito granular expandido a partir de glicerol
title Produção de hidrogênio e metabólitos em reator anaeróbio de leito fluidizado e em reator de leito granular expandido a partir de glicerol
spellingShingle Produção de hidrogênio e metabólitos em reator anaeróbio de leito fluidizado e em reator de leito granular expandido a partir de glicerol
Bosio, Morgana
TDH
Biodiesel
Temperatura mesofílica
Cultura mista
Metabólitos
HRT
Biodiesel
Mesophilic temperature
Mixed culture
Byproducts
ENGENHARIAS::ENGENHARIA QUIMICA
title_short Produção de hidrogênio e metabólitos em reator anaeróbio de leito fluidizado e em reator de leito granular expandido a partir de glicerol
title_full Produção de hidrogênio e metabólitos em reator anaeróbio de leito fluidizado e em reator de leito granular expandido a partir de glicerol
title_fullStr Produção de hidrogênio e metabólitos em reator anaeróbio de leito fluidizado e em reator de leito granular expandido a partir de glicerol
title_full_unstemmed Produção de hidrogênio e metabólitos em reator anaeróbio de leito fluidizado e em reator de leito granular expandido a partir de glicerol
title_sort Produção de hidrogênio e metabólitos em reator anaeróbio de leito fluidizado e em reator de leito granular expandido a partir de glicerol
author Bosio, Morgana
author_facet Bosio, Morgana
author_role author
dc.contributor.authorlattes.por.fl_str_mv http://lattes.cnpq.br/6639956330896050
dc.contributor.author.fl_str_mv Bosio, Morgana
dc.contributor.advisor1.fl_str_mv Silva, Edson Luiz
dc.contributor.advisor1Lattes.fl_str_mv http://lattes.cnpq.br/9720274214573371
contributor_str_mv Silva, Edson Luiz
dc.subject.por.fl_str_mv TDH
Biodiesel
Temperatura mesofílica
Cultura mista
Metabólitos
topic TDH
Biodiesel
Temperatura mesofílica
Cultura mista
Metabólitos
HRT
Biodiesel
Mesophilic temperature
Mixed culture
Byproducts
ENGENHARIAS::ENGENHARIA QUIMICA
dc.subject.eng.fl_str_mv HRT
Biodiesel
Mesophilic temperature
Mixed culture
Byproducts
dc.subject.cnpq.fl_str_mv ENGENHARIAS::ENGENHARIA QUIMICA
description This work aimed to evaluated the biological hydrogen production using crude glycerol as feedstock in two anaerobic reactors: (1) anaerobic fluidized bed reactor (AFBR), that allows high mass transfer, and (2) an expanded granular sludge blanket reactor, that can used with high efficiency even at high organic loading. In the AFBR, it was evaluated the influence of HRT (14, 12, 10, 8, 6, 4, 2 and 1 hour) in the hydrogen production using crude glycerol as feedstock at 5 g.L-1 and expanded clay as support material. In the EGSB, the HRT varied from 24 to 1 hour, it was used the same feedstock as that used in the AFBR. The reactors were maintained at controlled temperature at 30°C. The noculum for AFBR and EGSB was granular sludge taken from UASB reactor treating poultry slaughterhouse that was previously submitted to heat treatment. In the AFBR, the hydrogen production rate (HPR) increased from 0.08 to 0.73L.h-1.L -1 with the decrease at HRT from 14 to 1 hour, respectively. The hydrogen yield (HY) did not presented the same trend and remained almost unchanged (0.62, 0.76, 0.73, 0.75, 0.60, 0.58, 0.69, 0.85 molH2.mol-1glycerol). For this reactor, the main byproducts were 1,3-propanediol (1,3-PD), ethanol, acetic, butyric and propionic acid. The highest 1,3-PD (1,230 mg.L-1), ethanol (723 mg.L-1), acetic acid (204 mg.L-1), propionic acid (759 mg.L-1) and butyric acid (324 mg.L-1) concentration occurred at HRT of 6, 14, 8, 2, 6 hours, respectively. In the EGSB, the HPR and the HY presented the same trend: HPR increased from 0.018 to 1.708 L.h-1.L-1 and HY increased from 0.19 to 2.87 molH2.mol-1glycerol with the decrease in the HRT from 14 to 1 hour. For both reactors, the AFBR and the EGSB,the highest HPR and HY occurred at HRT of 1 hour. As well as for the AFBR, the main byproducts quantified in the EGSB were 1,3-propanediol (1,3-PD), ethanol, acetic, butyric and propionic acid. The highest 1,3-PD (1,606 mg.L -1), ethanol (400 mg.L-1), acetic acid (219 mg.L-1), propionic acid (1,075 mg.L-1) and butyric acid (248 mg.L-1) concentration occurred at HRT of 16, 12, 16, 8, 20 hours, respectively.
publishDate 2014
dc.date.issued.fl_str_mv 2014-03-28
dc.date.accessioned.fl_str_mv 2016-09-21T18:32:00Z
dc.date.available.fl_str_mv 2016-09-21T18:32:00Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/masterThesis
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dc.identifier.citation.fl_str_mv BOSIO, Morgana. Produção de hidrogênio e metabólitos em reator anaeróbio de leito fluidizado e em reator de leito granular expandido a partir de glicerol. 2014. Dissertação (Mestrado em Engenharia Química) – Universidade Federal de São Carlos, São Carlos, 2014. Disponível em: https://repositorio.ufscar.br/handle/ufscar/7361.
dc.identifier.uri.fl_str_mv https://repositorio.ufscar.br/handle/ufscar/7361
identifier_str_mv BOSIO, Morgana. Produção de hidrogênio e metabólitos em reator anaeróbio de leito fluidizado e em reator de leito granular expandido a partir de glicerol. 2014. Dissertação (Mestrado em Engenharia Química) – Universidade Federal de São Carlos, São Carlos, 2014. Disponível em: https://repositorio.ufscar.br/handle/ufscar/7361.
url https://repositorio.ufscar.br/handle/ufscar/7361
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dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
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dc.publisher.none.fl_str_mv Universidade Federal de São Carlos
Câmpus São Carlos
dc.publisher.program.fl_str_mv Programa de Pós-Graduação em Engenharia Química - PPGEQ
dc.publisher.initials.fl_str_mv UFSCar
publisher.none.fl_str_mv Universidade Federal de São Carlos
Câmpus São Carlos
dc.source.none.fl_str_mv reponame:Repositório Institucional da UFSCAR
instname:Universidade Federal de São Carlos (UFSCAR)
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instname_str Universidade Federal de São Carlos (UFSCAR)
instacron_str UFSCAR
institution UFSCAR
reponame_str Repositório Institucional da UFSCAR
collection Repositório Institucional da UFSCAR
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