Produção de ácido glucônico e xarope de frutose a partir de sacarose catalisada por enzimas em reator airlift

Detalhes bibliográficos
Autor(a) principal: Mafra, Agnes Cristina Oliveira
Data de Publicação: 2013
Tipo de documento: Dissertação
Idioma: por
Título da fonte: Repositório Institucional da UFSCAR
Texto Completo: https://repositorio.ufscar.br/handle/ufscar/4114
Resumo: The sugarcane sugar (sucrose) is a raw material produced in abundance in Brazil, being attractive to produce high added-value by-products. The gluconic acid (GA) can be obtained by multienzymatic conversion of sucrose, using three enzymes. Invertase, responsible for the inversion of sucrose to glucose and fructose, glucose oxidase (GOD) responsible for the glucose oxidation and catalase (CAT) responsible for decomposition of hydrogen peroxide. In multienzymatic process fructose is obtained as a byproduct, also of great interest to the food, pharmaceutical and chemical industries. In this study, the production of GA from sucrose in airlift reactor is evaluated. Temperature and pH of maximum activity were determined for the enzymes invertase, GOD and CAT , as well as the thermal stability in the absence of substrate. Invertase enzymatic activity was quantified by formation of reducing sugars on a 200 mM sucrose solution at 30 ° C, and pH 4.8. The enzymatic activity of GOD and the CAT were determined by monitoring respectively the formation of H2O2 from a solution of glucose 1 g/L, 25°C, pH 5.0 and the decomposition of H2O2 from a solution of H2O2 35 mM, 25°C, pH 7.5. Invertase showed maximum activity at 45 ºC and pH 5.0; GOD at 55ºC and pH 6.0 and CAT at 25 ° C and pH 8.0, respectively. From the activity profiles as a function of temperature and pH, the operational conditions of 50, 45 and 40°C at pH 5.0 and 6.0 were pre-selected for the multienzymatic process. It was found that the best half-lives times of the soluble enzymes, invertase, GOD and CAT, occurred in the condition of 40°C and pH 6.0, respectively 137, 105 and 98 h. A kinetic study was carried out at 40°C and pH 6.0. The kinetics of the enzyme invertase showed a behavior best predicted by the model of substrate inhibition. Michaelis-Menten model (MM) was fitted to experimental data of GOD and substrate inhibition model best predicted the kinetics behavior of CAT. The proposed kinetic models were used to estimate enzyme/substrate ratio (w/w) used in the production of GA in agitated and aerated and airlift bioreactors. On the other hand, in the batch assays conducted in airlift bioreactor were obtained AG real yields of 80.38 ± 5.69% and global yields of 103.20 ± 13.96% and conversion of sucrose of 98.86 ± 0.97%; obtained after 5 h. A new set of kinetic parameters including volumetric oxygen transfer coefficient (kLa) was based on the experimental data from tests in airlift bioreactor. These showed that Bi-Bi Ping-Pong model both with or without product inhibition correspond satisfactorily to the tendency of the experimental data.
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spelling Mafra, Agnes Cristina OliveiraTardioli, Paulo Waldirhttp://genos.cnpq.br:12010/dwlattes/owa/prc_imp_cv_int?f_cod=K4790436Z8http://lattes.cnpq.br/6868423702339380845df6ca-4e8f-4a52-becf-f23d76fcd9392016-06-02T19:56:50Z2013-04-262016-06-02T19:56:50Z2013-03-21MAFRA, Agnes Cristina Oliveira. Produção de ácido glucônico e xarope de frutose a partir de sacarose catalisada por enzimas em reator airlift. 2013. 122 f. Dissertação (Mestrado em Ciências Exatas e da Terra) - Universidade Federal de São Carlos, São Carlos, 2013.https://repositorio.ufscar.br/handle/ufscar/4114The sugarcane sugar (sucrose) is a raw material produced in abundance in Brazil, being attractive to produce high added-value by-products. The gluconic acid (GA) can be obtained by multienzymatic conversion of sucrose, using three enzymes. Invertase, responsible for the inversion of sucrose to glucose and fructose, glucose oxidase (GOD) responsible for the glucose oxidation and catalase (CAT) responsible for decomposition of hydrogen peroxide. In multienzymatic process fructose is obtained as a byproduct, also of great interest to the food, pharmaceutical and chemical industries. In this study, the production of GA from sucrose in airlift reactor is evaluated. Temperature and pH of maximum activity were determined for the enzymes invertase, GOD and CAT , as well as the thermal stability in the absence of substrate. Invertase enzymatic activity was quantified by formation of reducing sugars on a 200 mM sucrose solution at 30 ° C, and pH 4.8. The enzymatic activity of GOD and the CAT were determined by monitoring respectively the formation of H2O2 from a solution of glucose 1 g/L, 25°C, pH 5.0 and the decomposition of H2O2 from a solution of H2O2 35 mM, 25°C, pH 7.5. Invertase showed maximum activity at 45 ºC and pH 5.0; GOD at 55ºC and pH 6.0 and CAT at 25 ° C and pH 8.0, respectively. From the activity profiles as a function of temperature and pH, the operational conditions of 50, 45 and 40°C at pH 5.0 and 6.0 were pre-selected for the multienzymatic process. It was found that the best half-lives times of the soluble enzymes, invertase, GOD and CAT, occurred in the condition of 40°C and pH 6.0, respectively 137, 105 and 98 h. A kinetic study was carried out at 40°C and pH 6.0. The kinetics of the enzyme invertase showed a behavior best predicted by the model of substrate inhibition. Michaelis-Menten model (MM) was fitted to experimental data of GOD and substrate inhibition model best predicted the kinetics behavior of CAT. The proposed kinetic models were used to estimate enzyme/substrate ratio (w/w) used in the production of GA in agitated and aerated and airlift bioreactors. On the other hand, in the batch assays conducted in airlift bioreactor were obtained AG real yields of 80.38 ± 5.69% and global yields of 103.20 ± 13.96% and conversion of sucrose of 98.86 ± 0.97%; obtained after 5 h. A new set of kinetic parameters including volumetric oxygen transfer coefficient (kLa) was based on the experimental data from tests in airlift bioreactor. These showed that Bi-Bi Ping-Pong model both with or without product inhibition correspond satisfactorily to the tendency of the experimental data.O açúcar de cana (sacarose) é uma matéria-prima produzida em abundância no Brasil, sendo atrativa a produção de derivados com maior valor agregado. O ácido glucônico (AG) pode ser obtido através da conversão multienzimática da sacarose, utilizando como biocatalisadores as enzimas invertase, glicose oxidase (GOD) e catalase (CAT), responsáveis respectivamente pela inversão da sacarose, oxidação da glicose e decomposição de peróxido de hidrogênio (H2O2). No processo multienzimático obtém-se como subproduto a frutose, também de grande interesse para as indústrias alimentícia, farmacêutica e química. No presente trabalho foi avaliada a produção de AG a partir de sacarose em reator airlift. As enzimas invertase, GOD e CAT solúveis foram caracterizadas quanto à temperatura e ao pH de máxima atividade, bem como quanto à estabilidade térmica na ausência de substrato. A atividade enzimática da invertase foi quantificada pela ação da invertase sobre uma solução de sacarose 200 mM a 30ºC, pH 4,8, acompanhando-se a formação de açúcares redutores totais. As atividades enzimáticas da GOD e da CAT foram determinadas monitorando respectivamente a formação de H2O2 a partir de uma solução de glicose 1 g/l, 25ºC, pH 5,0 e a decomposição de H2O2 a partir de uma solução de H2O2 35 mM, 25ºC, pH 7,5. Invertase apresentou máxima atividade a 45ºC e pH 5,0; GOD a 55ºC e pH 6,0 e CAT a 25ºC e pH 8,0, respectivamente. A partir dos perfis de atividade em função da temperatura e do pH, as condições operacionais de 50, 45 e 40ºC em pHs 5,0 e 6,0 foram pré-selecionadas para a bioconversão multienzimática de sacarose a AG. Verificou-se que os melhores tempos de meias-vidas das enzimas invertase, GOD e CAT solúveis ocorreram na condição de 40ºC e pH 6,0, respectivamente 137, 105 e 98 h. Um estudo cinético foi realizado a 40ºC e pH 6,0. A cinética da enzima invertase apresentou comportamento previsto pelo modelo de inibição pelo substrato. O modelo de Michaelis-Menten (MM) foi ajustado aos dados experimentais da GOD e o modelo de inibição pelo substrato foi o que melhor se ajustou à cinética da CAT. Os modelos cinéticos propostos serviram para a estimativa das relações enzima/substrato (m.m-1) empregadas na produção de ácido glucônico em biorreatores agitado e aerado e airlift. Os ensaios em batelada em biorreator airlift apresentaram eficiências real e global em AG de respectivamente 80,40 ± 5,70 % e 103,20 ± 13,96 % e conversão de sacarose de 98,86 ± 0,97 %; obtidas após 5 h. Um novo ajuste dos parâmetros cinéticos incluindo o coeficiente volumétrico de transferência de oxigênio (kLa) foi realizado com base nos dados experimentais dos ensaios em biorreator airlift. Este mostrou que os modelos Bi-Bi Ping-Pong com ou sem inibição pelo produto responderam de forma satisfatória à tendência dos dados experimentais.Universidade Federal de Sao Carlosapplication/pdfporUniversidade Federal de São CarlosPrograma de Pós-Graduação em Engenharia Química - PPGEQUFSCarBREngenharia químicaSacaroseFrutoseÁcido glucônicoInvertaseCatalaseGlicose oxidaseAirlift.SucroseFructoseGluconic acidInvertaseGlucose oxidaseCatalaseAirliftENGENHARIAS::ENGENHARIA QUIMICAProdução de ácido glucônico e xarope de frutose a partir de sacarose catalisada por enzimas em reator airliftinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/masterThesis-1-157a91b28-06b2-4fc7-b127-2a5005569c49info:eu-repo/semantics/openAccessreponame:Repositório Institucional da UFSCARinstname:Universidade Federal de São Carlos (UFSCAR)instacron:UFSCARORIGINAL5040.pdfapplication/pdf2753762https://repositorio.ufscar.br/bitstream/ufscar/4114/1/5040.pdf183de6a78d0f606bfd3485cc5c3d7711MD51TEXT5040.pdf.txt5040.pdf.txtExtracted texttext/plain0https://repositorio.ufscar.br/bitstream/ufscar/4114/2/5040.pdf.txtd41d8cd98f00b204e9800998ecf8427eMD52THUMBNAIL5040.pdf.jpg5040.pdf.jpgIM Thumbnailimage/jpeg7638https://repositorio.ufscar.br/bitstream/ufscar/4114/3/5040.pdf.jpgb1ad3f3896d22b8591c2a3ac4b993e7bMD53ufscar/41142023-09-18 18:31:44.266oai:repositorio.ufscar.br:ufscar/4114Repositório InstitucionalPUBhttps://repositorio.ufscar.br/oai/requestopendoar:43222023-09-18T18:31:44Repositório Institucional da UFSCAR - Universidade Federal de São Carlos (UFSCAR)false
dc.title.por.fl_str_mv Produção de ácido glucônico e xarope de frutose a partir de sacarose catalisada por enzimas em reator airlift
title Produção de ácido glucônico e xarope de frutose a partir de sacarose catalisada por enzimas em reator airlift
spellingShingle Produção de ácido glucônico e xarope de frutose a partir de sacarose catalisada por enzimas em reator airlift
Mafra, Agnes Cristina Oliveira
Engenharia química
Sacarose
Frutose
Ácido glucônico
Invertase
Catalase
Glicose oxidase
Airlift.
Sucrose
Fructose
Gluconic acid
Invertase
Glucose oxidase
Catalase
Airlift
ENGENHARIAS::ENGENHARIA QUIMICA
title_short Produção de ácido glucônico e xarope de frutose a partir de sacarose catalisada por enzimas em reator airlift
title_full Produção de ácido glucônico e xarope de frutose a partir de sacarose catalisada por enzimas em reator airlift
title_fullStr Produção de ácido glucônico e xarope de frutose a partir de sacarose catalisada por enzimas em reator airlift
title_full_unstemmed Produção de ácido glucônico e xarope de frutose a partir de sacarose catalisada por enzimas em reator airlift
title_sort Produção de ácido glucônico e xarope de frutose a partir de sacarose catalisada por enzimas em reator airlift
author Mafra, Agnes Cristina Oliveira
author_facet Mafra, Agnes Cristina Oliveira
author_role author
dc.contributor.authorlattes.por.fl_str_mv http://lattes.cnpq.br/6868423702339380
dc.contributor.author.fl_str_mv Mafra, Agnes Cristina Oliveira
dc.contributor.advisor1.fl_str_mv Tardioli, Paulo Waldir
dc.contributor.advisor1Lattes.fl_str_mv http://genos.cnpq.br:12010/dwlattes/owa/prc_imp_cv_int?f_cod=K4790436Z8
dc.contributor.authorID.fl_str_mv 845df6ca-4e8f-4a52-becf-f23d76fcd939
contributor_str_mv Tardioli, Paulo Waldir
dc.subject.por.fl_str_mv Engenharia química
Sacarose
Frutose
Ácido glucônico
Invertase
Catalase
Glicose oxidase
Airlift.
topic Engenharia química
Sacarose
Frutose
Ácido glucônico
Invertase
Catalase
Glicose oxidase
Airlift.
Sucrose
Fructose
Gluconic acid
Invertase
Glucose oxidase
Catalase
Airlift
ENGENHARIAS::ENGENHARIA QUIMICA
dc.subject.eng.fl_str_mv Sucrose
Fructose
Gluconic acid
Invertase
Glucose oxidase
Catalase
Airlift
dc.subject.cnpq.fl_str_mv ENGENHARIAS::ENGENHARIA QUIMICA
description The sugarcane sugar (sucrose) is a raw material produced in abundance in Brazil, being attractive to produce high added-value by-products. The gluconic acid (GA) can be obtained by multienzymatic conversion of sucrose, using three enzymes. Invertase, responsible for the inversion of sucrose to glucose and fructose, glucose oxidase (GOD) responsible for the glucose oxidation and catalase (CAT) responsible for decomposition of hydrogen peroxide. In multienzymatic process fructose is obtained as a byproduct, also of great interest to the food, pharmaceutical and chemical industries. In this study, the production of GA from sucrose in airlift reactor is evaluated. Temperature and pH of maximum activity were determined for the enzymes invertase, GOD and CAT , as well as the thermal stability in the absence of substrate. Invertase enzymatic activity was quantified by formation of reducing sugars on a 200 mM sucrose solution at 30 ° C, and pH 4.8. The enzymatic activity of GOD and the CAT were determined by monitoring respectively the formation of H2O2 from a solution of glucose 1 g/L, 25°C, pH 5.0 and the decomposition of H2O2 from a solution of H2O2 35 mM, 25°C, pH 7.5. Invertase showed maximum activity at 45 ºC and pH 5.0; GOD at 55ºC and pH 6.0 and CAT at 25 ° C and pH 8.0, respectively. From the activity profiles as a function of temperature and pH, the operational conditions of 50, 45 and 40°C at pH 5.0 and 6.0 were pre-selected for the multienzymatic process. It was found that the best half-lives times of the soluble enzymes, invertase, GOD and CAT, occurred in the condition of 40°C and pH 6.0, respectively 137, 105 and 98 h. A kinetic study was carried out at 40°C and pH 6.0. The kinetics of the enzyme invertase showed a behavior best predicted by the model of substrate inhibition. Michaelis-Menten model (MM) was fitted to experimental data of GOD and substrate inhibition model best predicted the kinetics behavior of CAT. The proposed kinetic models were used to estimate enzyme/substrate ratio (w/w) used in the production of GA in agitated and aerated and airlift bioreactors. On the other hand, in the batch assays conducted in airlift bioreactor were obtained AG real yields of 80.38 ± 5.69% and global yields of 103.20 ± 13.96% and conversion of sucrose of 98.86 ± 0.97%; obtained after 5 h. A new set of kinetic parameters including volumetric oxygen transfer coefficient (kLa) was based on the experimental data from tests in airlift bioreactor. These showed that Bi-Bi Ping-Pong model both with or without product inhibition correspond satisfactorily to the tendency of the experimental data.
publishDate 2013
dc.date.available.fl_str_mv 2013-04-26
2016-06-02T19:56:50Z
dc.date.issued.fl_str_mv 2013-03-21
dc.date.accessioned.fl_str_mv 2016-06-02T19:56:50Z
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dc.identifier.citation.fl_str_mv MAFRA, Agnes Cristina Oliveira. Produção de ácido glucônico e xarope de frutose a partir de sacarose catalisada por enzimas em reator airlift. 2013. 122 f. Dissertação (Mestrado em Ciências Exatas e da Terra) - Universidade Federal de São Carlos, São Carlos, 2013.
dc.identifier.uri.fl_str_mv https://repositorio.ufscar.br/handle/ufscar/4114
identifier_str_mv MAFRA, Agnes Cristina Oliveira. Produção de ácido glucônico e xarope de frutose a partir de sacarose catalisada por enzimas em reator airlift. 2013. 122 f. Dissertação (Mestrado em Ciências Exatas e da Terra) - Universidade Federal de São Carlos, São Carlos, 2013.
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dc.publisher.country.fl_str_mv BR
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