Production of dextransucrase, dextran and fructose from sucrose using Leuconostoc mesenteroides NRRL B512(f)

Detalhes bibliográficos
Autor(a) principal: Santos, Mariana
Data de Publicação: 2000
Outros Autores: Teixeira, J. A., Rodrigues, Alírio
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos)
Texto Completo: http://hdl.handle.net/1822/1827
Resumo: The production of dextransucrase, dextran and fructose by sucrose fermentation using Leuconostoc mesenteroides NRRL-B512(F) was studied in batch operation in a bioreactor with total working volume of 1.5 dm³. The effect of temperature (20 to 40ºC), pH (5.5 and 6.7) and sucrose concentration (10 to 120 g/l) on process performance was studied. The optimum conditions for dextran and fructose production were T=35ºC and pH=5.5. Cell growth is not inhibited by high sucrose concentrations; however, for sucrose concentration higher than 40 g/dm³ separation of products from cells is difficult. Biomass (X), enzyme (E), dextran (D), fructose (F) and sucrose (S) rate equations were considered in order to derive a simple fermentation kinetic model from batch experimental data. The logistic equation provided a reasonable description for cell concentration,X. The Luedeking and Piret equation was used to describe the enzyme production rate, by considering only the growth associated term. The concentrations of products (dextran and fructose) were reasonably described by a first order kinetic law with respect to both substrate and enzyme concentrations; the substrate, S was consumed for cell growth and for dextran and fructose production. Model parameters µ_m and X_o were calculated from cell growth as a function of time. The yield Y_E/X were calculated from X_max and E_max and Y_X/S was estimated from X_max and the sucrose consumed by the bacteria. The remaining parameter k' was obtained by fitting the experimental data of substrate, dextran and fructose concentrations versus time.
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spelling Production of dextransucrase, dextran and fructose from sucrose using Leuconostoc mesenteroides NRRL B512(f)Leuconostoc mesenteroidesDextransucraseDextranFructoseBatch fermentationKineticModellingThe production of dextransucrase, dextran and fructose by sucrose fermentation using Leuconostoc mesenteroides NRRL-B512(F) was studied in batch operation in a bioreactor with total working volume of 1.5 dm³. The effect of temperature (20 to 40ºC), pH (5.5 and 6.7) and sucrose concentration (10 to 120 g/l) on process performance was studied. The optimum conditions for dextran and fructose production were T=35ºC and pH=5.5. Cell growth is not inhibited by high sucrose concentrations; however, for sucrose concentration higher than 40 g/dm³ separation of products from cells is difficult. Biomass (X), enzyme (E), dextran (D), fructose (F) and sucrose (S) rate equations were considered in order to derive a simple fermentation kinetic model from batch experimental data. The logistic equation provided a reasonable description for cell concentration,X. The Luedeking and Piret equation was used to describe the enzyme production rate, by considering only the growth associated term. The concentrations of products (dextran and fructose) were reasonably described by a first order kinetic law with respect to both substrate and enzyme concentrations; the substrate, S was consumed for cell growth and for dextran and fructose production. Model parameters µ_m and X_o were calculated from cell growth as a function of time. The yield Y_E/X were calculated from X_max and E_max and Y_X/S was estimated from X_max and the sucrose consumed by the bacteria. The remaining parameter k' was obtained by fitting the experimental data of substrate, dextran and fructose concentrations versus time.Fundação para a Ciência e a Tecnologia (FCT) – Praxis XXI - BD/5004/95.Programa IberoAmericano de Ciencia e Tecnología para el Desarrollo (CYTED) - programme IV.7.ElsevierUniversidade do MinhoSantos, MarianaTeixeira, J. A.Rodrigues, Alírio20002000-01-01T00:00:00Zinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleapplication/pdfhttp://hdl.handle.net/1822/1827eng“Biochemical engineering journal”. ISSN 1369-703X. 4:3 (2000) 177-188.1369-703Xinfo: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:RCAAP2023-07-21T12:51:10Zoai:repositorium.sdum.uminho.pt:1822/1827Portal AgregadorONGhttps://www.rcaap.pt/oai/openaireopendoar:71602024-03-19T19:50:01.270122Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) - Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informaçãofalse
dc.title.none.fl_str_mv Production of dextransucrase, dextran and fructose from sucrose using Leuconostoc mesenteroides NRRL B512(f)
title Production of dextransucrase, dextran and fructose from sucrose using Leuconostoc mesenteroides NRRL B512(f)
spellingShingle Production of dextransucrase, dextran and fructose from sucrose using Leuconostoc mesenteroides NRRL B512(f)
Santos, Mariana
Leuconostoc mesenteroides
Dextransucrase
Dextran
Fructose
Batch fermentation
Kinetic
Modelling
title_short Production of dextransucrase, dextran and fructose from sucrose using Leuconostoc mesenteroides NRRL B512(f)
title_full Production of dextransucrase, dextran and fructose from sucrose using Leuconostoc mesenteroides NRRL B512(f)
title_fullStr Production of dextransucrase, dextran and fructose from sucrose using Leuconostoc mesenteroides NRRL B512(f)
title_full_unstemmed Production of dextransucrase, dextran and fructose from sucrose using Leuconostoc mesenteroides NRRL B512(f)
title_sort Production of dextransucrase, dextran and fructose from sucrose using Leuconostoc mesenteroides NRRL B512(f)
author Santos, Mariana
author_facet Santos, Mariana
Teixeira, J. A.
Rodrigues, Alírio
author_role author
author2 Teixeira, J. A.
Rodrigues, Alírio
author2_role author
author
dc.contributor.none.fl_str_mv Universidade do Minho
dc.contributor.author.fl_str_mv Santos, Mariana
Teixeira, J. A.
Rodrigues, Alírio
dc.subject.por.fl_str_mv Leuconostoc mesenteroides
Dextransucrase
Dextran
Fructose
Batch fermentation
Kinetic
Modelling
topic Leuconostoc mesenteroides
Dextransucrase
Dextran
Fructose
Batch fermentation
Kinetic
Modelling
description The production of dextransucrase, dextran and fructose by sucrose fermentation using Leuconostoc mesenteroides NRRL-B512(F) was studied in batch operation in a bioreactor with total working volume of 1.5 dm³. The effect of temperature (20 to 40ºC), pH (5.5 and 6.7) and sucrose concentration (10 to 120 g/l) on process performance was studied. The optimum conditions for dextran and fructose production were T=35ºC and pH=5.5. Cell growth is not inhibited by high sucrose concentrations; however, for sucrose concentration higher than 40 g/dm³ separation of products from cells is difficult. Biomass (X), enzyme (E), dextran (D), fructose (F) and sucrose (S) rate equations were considered in order to derive a simple fermentation kinetic model from batch experimental data. The logistic equation provided a reasonable description for cell concentration,X. The Luedeking and Piret equation was used to describe the enzyme production rate, by considering only the growth associated term. The concentrations of products (dextran and fructose) were reasonably described by a first order kinetic law with respect to both substrate and enzyme concentrations; the substrate, S was consumed for cell growth and for dextran and fructose production. Model parameters µ_m and X_o were calculated from cell growth as a function of time. The yield Y_E/X were calculated from X_max and E_max and Y_X/S was estimated from X_max and the sucrose consumed by the bacteria. The remaining parameter k' was obtained by fitting the experimental data of substrate, dextran and fructose concentrations versus time.
publishDate 2000
dc.date.none.fl_str_mv 2000
2000-01-01T00:00:00Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/article
format article
status_str publishedVersion
dc.identifier.uri.fl_str_mv http://hdl.handle.net/1822/1827
url http://hdl.handle.net/1822/1827
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv “Biochemical engineering journal”. ISSN 1369-703X. 4:3 (2000) 177-188.
1369-703X
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.publisher.none.fl_str_mv Elsevier
publisher.none.fl_str_mv Elsevier
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 Repositório Científico de Acesso Aberto de Portugal (Repositórios Cientìficos) - Agência para a Sociedade do Conhecimento (UMIC) - FCT - Sociedade da Informação
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