Produção biotecnólogica de ácido succínico a partir de casca de arroz

Detalhes bibliográficos
Ano de defesa: 2013
Autor(a) principal: Bevilaqua, Daiane Balconi lattes
Orientador(a): Martins, Ayrton Figueiredo lattes
Banca de defesa: Oliveira, Elizangela Gonçalves de lattes, Carissimi, Elvis lattes, Dallago, Rogério Marcos lattes, Richards, Neila Silvia Pereira dos Santos lattes
Tipo de documento: Tese
Tipo de acesso: Acesso aberto
Idioma: por
Instituição de defesa: Universidade Federal de Santa Maria
Programa de Pós-Graduação: Programa de Pós-Graduação em Química
Departamento: Química
País: BR
Palavras-chave em Português:
Palavras-chave em Inglês:
Área do conhecimento CNPq:
Link de acesso: http://repositorio.ufsm.br/handle/1/4260
Resumo: Rice husk is a subproduct of the food industry, rich in carbohydrates, which can be partially fractionated and converted into fermentable sugars. In this work, it was investigated the best conditions for the conversion of the residual biomass, rice husks, into succinic acid, an important start molecule for the synthesis of the chemo-pharmaceutical industry. With the goal of the separation of lignin and transformation of cellulose and hemicellulose into sugars, the rice husks were submitted, initially, to acid hydrolysis, in autoclave and in pressurized polytetrafluoroethylene reactor. The hydrolysis conditions were optimized by factorial design for the pressurized acid hydrolysis; temperature, time and acid catalyst concentration (HCl or H2SO4) were evaluated. For the acid hydrolysis in autoclave, it was optimized the ratio rice husks mass: acid volume, time and concentration of HCl or H2SO4. It was observed that the sugar production by using autoclave was lower than by the pressurized hydrolysis system, needing further concentration of the hydrolysate for the subsequent fermentation step. The best results were obtained with the polytetrafluoroethylene reactor, by 59 bar, with HCl 0,26 mol L-1, at 175°C and reaction time of 46 min, yielding 19.0 g L- 1 of glucose and 3.01 g L- 1 of xylose. The efficiency of different detoxification methods of the hydrolyzed rice husk were evaluated; the combined method of pH adjustment plus adsorption on active carbon was the most effective by eliminating inhibitors, without appreciable reduction of the sugar concentration. The detoxified hydrolysate was sterilized and adjusted at pH 7 and fermented with A. succinogenes at 37 ° C, in anaerobic medium, occurring the conversion of the two main monosaccharides, glucose and xylose, into succinic acid. The nutrient concentration and the agitation rate of the medium were also optimized by factorial design. As a result, after 54 h of static fermentation, the hydrolysate was supplemented with 8.40 g L-1 yeast extract and 1.40 g L -1 of NaHCO3, to yield 59.9% succinic acid. Almost all of the sugar at this time was consumed and converted to succinic acid; at the same time, acetic and formic acid are formed, but, in low concentrations related to the production of succinic acid, not compromising the yield of the process. For the succinic acid extraction and purification, the fermentate was submitted to the solid phase extraction procedure; cartridges with different extraction phases were tested, and among them, the ion exchange one was the only effective, with recoveries up to 96%. After solid phase extraction, the eluted solution, containing 12.05 g L- 1 succcinic acid, was lyophilized, and crystals of succinic acid with 80.7% (m m- 1) were obtained. The raw material used in the bioprocess has no commercial value, representing a zero cost carbon source, which reveals itself adequate to the succinic acid production by fermentation with A. succinogenes, after hydrolysis. The use of the residual rice husk can contribute to the mitigation of the environmental impact resulting from the illegal discharge in the environment.
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spelling 2017-05-122017-05-122013-12-16BEVILAQUA, Daiane Balconi. Biotecnological production of succinic acid from rice husks. 2013. 124 f. Tese (Doutorado em Química) - Universidade Federal de Santa Maria, Santa Maria, 2013.http://repositorio.ufsm.br/handle/1/4260Rice husk is a subproduct of the food industry, rich in carbohydrates, which can be partially fractionated and converted into fermentable sugars. In this work, it was investigated the best conditions for the conversion of the residual biomass, rice husks, into succinic acid, an important start molecule for the synthesis of the chemo-pharmaceutical industry. With the goal of the separation of lignin and transformation of cellulose and hemicellulose into sugars, the rice husks were submitted, initially, to acid hydrolysis, in autoclave and in pressurized polytetrafluoroethylene reactor. The hydrolysis conditions were optimized by factorial design for the pressurized acid hydrolysis; temperature, time and acid catalyst concentration (HCl or H2SO4) were evaluated. For the acid hydrolysis in autoclave, it was optimized the ratio rice husks mass: acid volume, time and concentration of HCl or H2SO4. It was observed that the sugar production by using autoclave was lower than by the pressurized hydrolysis system, needing further concentration of the hydrolysate for the subsequent fermentation step. The best results were obtained with the polytetrafluoroethylene reactor, by 59 bar, with HCl 0,26 mol L-1, at 175°C and reaction time of 46 min, yielding 19.0 g L- 1 of glucose and 3.01 g L- 1 of xylose. The efficiency of different detoxification methods of the hydrolyzed rice husk were evaluated; the combined method of pH adjustment plus adsorption on active carbon was the most effective by eliminating inhibitors, without appreciable reduction of the sugar concentration. The detoxified hydrolysate was sterilized and adjusted at pH 7 and fermented with A. succinogenes at 37 ° C, in anaerobic medium, occurring the conversion of the two main monosaccharides, glucose and xylose, into succinic acid. The nutrient concentration and the agitation rate of the medium were also optimized by factorial design. As a result, after 54 h of static fermentation, the hydrolysate was supplemented with 8.40 g L-1 yeast extract and 1.40 g L -1 of NaHCO3, to yield 59.9% succinic acid. Almost all of the sugar at this time was consumed and converted to succinic acid; at the same time, acetic and formic acid are formed, but, in low concentrations related to the production of succinic acid, not compromising the yield of the process. For the succinic acid extraction and purification, the fermentate was submitted to the solid phase extraction procedure; cartridges with different extraction phases were tested, and among them, the ion exchange one was the only effective, with recoveries up to 96%. After solid phase extraction, the eluted solution, containing 12.05 g L- 1 succcinic acid, was lyophilized, and crystals of succinic acid with 80.7% (m m- 1) were obtained. The raw material used in the bioprocess has no commercial value, representing a zero cost carbon source, which reveals itself adequate to the succinic acid production by fermentation with A. succinogenes, after hydrolysis. The use of the residual rice husk can contribute to the mitigation of the environmental impact resulting from the illegal discharge in the environment.A casca de arroz é um subproduto da indústria de alimentos, rico em carboidratos, que pode ser fracionada e, parcialmente, convertida em açúcares fermentescíveis. Neste trabalho, investigou-se as melhores condições para a conversão da biomassa residual, casca de arroz, em ácido succínico, importante insumo para a síntese industrial farmoquímica. Com o objetivo de separação da lignina e transformação da celulose e da hemicelulose em açúcares, a casca de arroz foi submetida, inicialmente, à hidrólise ácida em autoclave e em reator de politetrafluoretileno, à pressão. As condições de hidrólise foram otimizadas através de planejamento fatorial, sendo avaliado na hidrólise ácida pressurizada, a influência da temperatura, do tempo e da concentração do catalisador ácido (HCl ou H2SO4); já, na hidrólise em autoclave, otimizou-se a relação massa de casca de arroz : volume de solução ácida, tempo e concentração de HCl ou H2SO4. Observou-se que a produção de açúcares em autoclave é inferior à do sistema de hidrólise à pressão, necessitando, inclusive, concentração do hidrolisado para utilização na etapa fermentativa. Os melhores resultados foram obtidos com o reator de politetrafluoretileno, à pressão de 59 bar, com 0,26 mol L-1 de HCl, temperatura de 175 °C e tempo de reação de 46 min, produzindo-se 19 g L-1 de glicose e 3,01 g L-1 de xilose. Avaliou-se a eficiência de diferentes métodos de destoxificação do hidrolisado de casca de arroz, sendo o método combinado, de ajuste de pH seguido de adsorção em carvão ativado, o mais eficaz na eliminação de inibidores, sem redução apreciável da concentração de açúcares. O hidrolisado destoxificado foi esterilizado, ajustado a pH 7 e fermentado com A. succinogenes, à 37 ºC, em meio anaeróbio, ocorrendo a conversão dos monossacarídeos predominantes, glicose e xilose, em ácido succínico. A concentração dos nutrientes e a velocidade de agitação do meio também foram otimizadas por meio de planejamento fatorial. Após 54 h de fermentação estática do hidrolisado, suplementado com 8,40 g L-1 de extrato de levedura e 1,40 g L-1 de NaHCO3, o rendimento em ácido succínico foi de 59,9%. Praticamente, toda a concentração de açúcar é consumida neste tempo e convertida em ácido succínico; simultaneamente, formam-se ácido acético e fórmico, porém, em baixas concentrações em relação à produção de ácido succínico, não comprometendo o rendimento do processo. Para a extração e purificação do ácido succínico, o fermentado foi submetido ao procedimento de extração em fase sólida; cartuchos com diferentes fases extratoras foram testados, e, dentre eles, somente o de troca iônica se mostrou efetivo, com recuperação de até 96,0%. Após a extração, o eluido da extração em fase sólida, contendo 12,0 g L-1 de ácido succínico foi liofilizado, obtendo-se cristais com pureza de 80,7% (m m-1). A matéria-prima utilizada no bioprocesso, casca de arroz, não tem valor comercial, representando fonte de carbono de custo zero, que se revelou adequada à produção de ácido succínico por meio de fermentação com A. succinogenes, após hidrólise. O aproveitamento da casca de arroz residual pode contribuir para a mitigação do impacto ambiental resultante da disposição ilegal no ambiente.Coordenação de Aperfeiçoamento de Pessoal de Nível Superiorapplication/pdfporUniversidade Federal de Santa MariaPrograma de Pós-Graduação em QuímicaUFSMBRQuímicaCasca de arrozHidrólise ácida pressurizadaA. succinogenesÁcido succínicoOtimização do processoRice husksPressurized acid hydrolysisA. succinogenesSuccinic acidOptimization processCNPQ::CIENCIAS EXATAS E DA TERRA::QUIMICAProdução biotecnólogica de ácido succínico a partir de casca de arrozBiotecnological production of succinic acid from rice husksinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/doctoralThesisMartins, Ayrton Figueiredohttp://lattes.cnpq.br/2113532494494821Oliveira, Elizangela Gonçalves dehttp://lattes.cnpq.br/1578951812092017Carissimi, Elvishttp://lattes.cnpq.br/4642912749433316Dallago, Rogério Marcoshttp://lattes.cnpq.br/3006526142468362Richards, Neila Silvia Pereira dos Santoshttp://lattes.cnpq.br/0618653776990780http://lattes.cnpq.br/3787674861849653Bevilaqua, Daiane Balconi100600000000400300300300300300500ade6000d-a348-4d49-a531-6500a65a153a486bc091-1e85-4d81-bbae-50f40b6604ad3778f147-7940-482c-b415-b28faf78b23ce17fa918-e6fc-4cc7-95ff-b1b504fb16a424ded0f7-6d99-4c39-997d-0e6db3f4407e17a21f77-88b4-4d77-8396-049941753c69info:eu-repo/semantics/openAccessreponame:Biblioteca Digital de Teses e Dissertações do UFSMinstname:Universidade Federal de Santa Maria (UFSM)instacron:UFSMORIGINALBEVILAQUA, DAIANE BALCONI.pdfapplication/pdf4426288http://repositorio.ufsm.br/bitstream/1/4260/1/BEVILAQUA%2c%20DAIANE%20BALCONI.pdf46dd0dd78299f450df24bd7f0585d357MD51TEXTBEVILAQUA, DAIANE BALCONI.pdf.txtBEVILAQUA, DAIANE BALCONI.pdf.txtExtracted texttext/plain195118http://repositorio.ufsm.br/bitstream/1/4260/2/BEVILAQUA%2c%20DAIANE%20BALCONI.pdf.txt03f061d09b5170a9922d67cfcd3fea91MD52THUMBNAILBEVILAQUA, DAIANE BALCONI.pdf.jpgBEVILAQUA, DAIANE BALCONI.pdf.jpgIM Thumbnailimage/jpeg4535http://repositorio.ufsm.br/bitstream/1/4260/3/BEVILAQUA%2c%20DAIANE%20BALCONI.pdf.jpg316b2723cc4bf7f8d79f9fb5c14e4242MD531/42602023-05-11 14:34:31.194oai:repositorio.ufsm.br:1/4260Biblioteca Digital de Teses e Dissertaçõeshttps://repositorio.ufsm.br/ONGhttps://repositorio.ufsm.br/oai/requestatendimento.sib@ufsm.br||tedebc@gmail.comopendoar:2023-05-11T17:34:31Biblioteca Digital de Teses e Dissertações do UFSM - Universidade Federal de Santa Maria (UFSM)false
dc.title.por.fl_str_mv Produção biotecnólogica de ácido succínico a partir de casca de arroz
dc.title.alternative.eng.fl_str_mv Biotecnological production of succinic acid from rice husks
title Produção biotecnólogica de ácido succínico a partir de casca de arroz
spellingShingle Produção biotecnólogica de ácido succínico a partir de casca de arroz
Bevilaqua, Daiane Balconi
Casca de arroz
Hidrólise ácida pressurizada
A. succinogenes
Ácido succínico
Otimização do processo
Rice husks
Pressurized acid hydrolysis
A. succinogenes
Succinic acid
Optimization process
CNPQ::CIENCIAS EXATAS E DA TERRA::QUIMICA
title_short Produção biotecnólogica de ácido succínico a partir de casca de arroz
title_full Produção biotecnólogica de ácido succínico a partir de casca de arroz
title_fullStr Produção biotecnólogica de ácido succínico a partir de casca de arroz
title_full_unstemmed Produção biotecnólogica de ácido succínico a partir de casca de arroz
title_sort Produção biotecnólogica de ácido succínico a partir de casca de arroz
author Bevilaqua, Daiane Balconi
author_facet Bevilaqua, Daiane Balconi
author_role author
dc.contributor.advisor1.fl_str_mv Martins, Ayrton Figueiredo
dc.contributor.advisor1Lattes.fl_str_mv http://lattes.cnpq.br/2113532494494821
dc.contributor.referee1.fl_str_mv Oliveira, Elizangela Gonçalves de
dc.contributor.referee1Lattes.fl_str_mv http://lattes.cnpq.br/1578951812092017
dc.contributor.referee2.fl_str_mv Carissimi, Elvis
dc.contributor.referee2Lattes.fl_str_mv http://lattes.cnpq.br/4642912749433316
dc.contributor.referee3.fl_str_mv Dallago, Rogério Marcos
dc.contributor.referee3Lattes.fl_str_mv http://lattes.cnpq.br/3006526142468362
dc.contributor.referee4.fl_str_mv Richards, Neila Silvia Pereira dos Santos
dc.contributor.referee4Lattes.fl_str_mv http://lattes.cnpq.br/0618653776990780
dc.contributor.authorLattes.fl_str_mv http://lattes.cnpq.br/3787674861849653
dc.contributor.author.fl_str_mv Bevilaqua, Daiane Balconi
contributor_str_mv Martins, Ayrton Figueiredo
Oliveira, Elizangela Gonçalves de
Carissimi, Elvis
Dallago, Rogério Marcos
Richards, Neila Silvia Pereira dos Santos
dc.subject.por.fl_str_mv Casca de arroz
Hidrólise ácida pressurizada
A. succinogenes
Ácido succínico
Otimização do processo
topic Casca de arroz
Hidrólise ácida pressurizada
A. succinogenes
Ácido succínico
Otimização do processo
Rice husks
Pressurized acid hydrolysis
A. succinogenes
Succinic acid
Optimization process
CNPQ::CIENCIAS EXATAS E DA TERRA::QUIMICA
dc.subject.eng.fl_str_mv Rice husks
Pressurized acid hydrolysis
A. succinogenes
Succinic acid
Optimization process
dc.subject.cnpq.fl_str_mv CNPQ::CIENCIAS EXATAS E DA TERRA::QUIMICA
description Rice husk is a subproduct of the food industry, rich in carbohydrates, which can be partially fractionated and converted into fermentable sugars. In this work, it was investigated the best conditions for the conversion of the residual biomass, rice husks, into succinic acid, an important start molecule for the synthesis of the chemo-pharmaceutical industry. With the goal of the separation of lignin and transformation of cellulose and hemicellulose into sugars, the rice husks were submitted, initially, to acid hydrolysis, in autoclave and in pressurized polytetrafluoroethylene reactor. The hydrolysis conditions were optimized by factorial design for the pressurized acid hydrolysis; temperature, time and acid catalyst concentration (HCl or H2SO4) were evaluated. For the acid hydrolysis in autoclave, it was optimized the ratio rice husks mass: acid volume, time and concentration of HCl or H2SO4. It was observed that the sugar production by using autoclave was lower than by the pressurized hydrolysis system, needing further concentration of the hydrolysate for the subsequent fermentation step. The best results were obtained with the polytetrafluoroethylene reactor, by 59 bar, with HCl 0,26 mol L-1, at 175°C and reaction time of 46 min, yielding 19.0 g L- 1 of glucose and 3.01 g L- 1 of xylose. The efficiency of different detoxification methods of the hydrolyzed rice husk were evaluated; the combined method of pH adjustment plus adsorption on active carbon was the most effective by eliminating inhibitors, without appreciable reduction of the sugar concentration. The detoxified hydrolysate was sterilized and adjusted at pH 7 and fermented with A. succinogenes at 37 ° C, in anaerobic medium, occurring the conversion of the two main monosaccharides, glucose and xylose, into succinic acid. The nutrient concentration and the agitation rate of the medium were also optimized by factorial design. As a result, after 54 h of static fermentation, the hydrolysate was supplemented with 8.40 g L-1 yeast extract and 1.40 g L -1 of NaHCO3, to yield 59.9% succinic acid. Almost all of the sugar at this time was consumed and converted to succinic acid; at the same time, acetic and formic acid are formed, but, in low concentrations related to the production of succinic acid, not compromising the yield of the process. For the succinic acid extraction and purification, the fermentate was submitted to the solid phase extraction procedure; cartridges with different extraction phases were tested, and among them, the ion exchange one was the only effective, with recoveries up to 96%. After solid phase extraction, the eluted solution, containing 12.05 g L- 1 succcinic acid, was lyophilized, and crystals of succinic acid with 80.7% (m m- 1) were obtained. The raw material used in the bioprocess has no commercial value, representing a zero cost carbon source, which reveals itself adequate to the succinic acid production by fermentation with A. succinogenes, after hydrolysis. The use of the residual rice husk can contribute to the mitigation of the environmental impact resulting from the illegal discharge in the environment.
publishDate 2013
dc.date.issued.fl_str_mv 2013-12-16
dc.date.accessioned.fl_str_mv 2017-05-12
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dc.identifier.citation.fl_str_mv BEVILAQUA, Daiane Balconi. Biotecnological production of succinic acid from rice husks. 2013. 124 f. Tese (Doutorado em Química) - Universidade Federal de Santa Maria, Santa Maria, 2013.
dc.identifier.uri.fl_str_mv http://repositorio.ufsm.br/handle/1/4260
identifier_str_mv BEVILAQUA, Daiane Balconi. Biotecnological production of succinic acid from rice husks. 2013. 124 f. Tese (Doutorado em Química) - Universidade Federal de Santa Maria, Santa Maria, 2013.
url http://repositorio.ufsm.br/handle/1/4260
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