Evaluation of different biological and chemical treatments in agroindustrial residues for the production of fungal glucanases and xylanases
Autor(a) principal: | |
---|---|
Data de Publicação: | 2018 |
Outros Autores: | , , , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Repositório Institucional da UNESP |
Texto Completo: | http://dx.doi.org/10.1016/j.procbio.2018.02.008 http://hdl.handle.net/11449/175900 |
Resumo: | The production and use of fibrolytic enzyme complex in the hydrolysis of lignocellulosic materials is an important strategy for renewable bioenergy. The different carbon sources (residues) with or without some pretreatments (biological or chemical) were analyzed in order to increase the production of fibrolytic enzyme. Glycosyl hydrolases and xylanases were produced using Trichoderma reesei QM9414. The influence of some crude or pre-treated agro-industrial residues as a carbon source was previously investigated using shake-flask cultures. Subsequently, the selection of the best culture medium was studied under different pH and temperature conditions in stirred tank bioreactor. Fibrolytic activities reached a maximum of 0.85 ± 0.07 FPU mL−1 (total cellulase), 3.14 ± 0.01 CMC mL−1 (endoglucanase) and 1.25 ± 0.14 U mL−1 (exoglucanase) with the orange peel residue; and 93.08 ± 3.27 U mL−1 (xylanase) with sugarcane bagasse under alkali pretreatment. In the stirred tank bioreactor the cellulolytic activity increased to 1.76 ± 0.00 FPU mL−1, about 2 times higher than in the shake-flasks or under studied conditions. The biosynthesis of the fibrolytic complex using agroindustrial residues supplemented was shown to reach a higher total cellulose production. |
id |
UNSP_d8c445a3260672bf8649f63d05544b96 |
---|---|
oai_identifier_str |
oai:repositorio.unesp.br:11449/175900 |
network_acronym_str |
UNSP |
network_name_str |
Repositório Institucional da UNESP |
repository_id_str |
2946 |
spelling |
Evaluation of different biological and chemical treatments in agroindustrial residues for the production of fungal glucanases and xylanasesFibrolytic enzyme complexShake-flask culturesStirred tank bioreactorSubmerged fermentation (SmF)Trichoderma reesei QM9414The production and use of fibrolytic enzyme complex in the hydrolysis of lignocellulosic materials is an important strategy for renewable bioenergy. The different carbon sources (residues) with or without some pretreatments (biological or chemical) were analyzed in order to increase the production of fibrolytic enzyme. Glycosyl hydrolases and xylanases were produced using Trichoderma reesei QM9414. The influence of some crude or pre-treated agro-industrial residues as a carbon source was previously investigated using shake-flask cultures. Subsequently, the selection of the best culture medium was studied under different pH and temperature conditions in stirred tank bioreactor. Fibrolytic activities reached a maximum of 0.85 ± 0.07 FPU mL−1 (total cellulase), 3.14 ± 0.01 CMC mL−1 (endoglucanase) and 1.25 ± 0.14 U mL−1 (exoglucanase) with the orange peel residue; and 93.08 ± 3.27 U mL−1 (xylanase) with sugarcane bagasse under alkali pretreatment. In the stirred tank bioreactor the cellulolytic activity increased to 1.76 ± 0.00 FPU mL−1, about 2 times higher than in the shake-flasks or under studied conditions. The biosynthesis of the fibrolytic complex using agroindustrial residues supplemented was shown to reach a higher total cellulose production.Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)Biotechnology Department São Paulo State University UNESP CampusBiochemistry and Microbiology Department UNESP CampusBiotechnology Department São Paulo State University UNESP CampusBiochemistry and Microbiology Department UNESP CampusUniversidade Estadual Paulista (Unesp)Silva, D. F. [UNESP]Hergesel, L. M. [UNESP]Campioni, T. S. [UNESP]Carvalho, A. F.A. [UNESP]Oliva-Neto, P. [UNESP]2018-12-11T17:18:03Z2018-12-11T17:18:03Z2018-04-01info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/article29-37application/pdfhttp://dx.doi.org/10.1016/j.procbio.2018.02.008Process Biochemistry, v. 67, p. 29-37.1359-5113http://hdl.handle.net/11449/17590010.1016/j.procbio.2018.02.0082-s2.0-850421563822-s2.0-85042156382.pdfScopusreponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPengProcess Biochemistry0,761info:eu-repo/semantics/openAccess2023-11-06T06:12:09Zoai:repositorio.unesp.br:11449/175900Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462024-08-05T17:02:21.303039Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false |
dc.title.none.fl_str_mv |
Evaluation of different biological and chemical treatments in agroindustrial residues for the production of fungal glucanases and xylanases |
title |
Evaluation of different biological and chemical treatments in agroindustrial residues for the production of fungal glucanases and xylanases |
spellingShingle |
Evaluation of different biological and chemical treatments in agroindustrial residues for the production of fungal glucanases and xylanases Silva, D. F. [UNESP] Fibrolytic enzyme complex Shake-flask cultures Stirred tank bioreactor Submerged fermentation (SmF) Trichoderma reesei QM9414 |
title_short |
Evaluation of different biological and chemical treatments in agroindustrial residues for the production of fungal glucanases and xylanases |
title_full |
Evaluation of different biological and chemical treatments in agroindustrial residues for the production of fungal glucanases and xylanases |
title_fullStr |
Evaluation of different biological and chemical treatments in agroindustrial residues for the production of fungal glucanases and xylanases |
title_full_unstemmed |
Evaluation of different biological and chemical treatments in agroindustrial residues for the production of fungal glucanases and xylanases |
title_sort |
Evaluation of different biological and chemical treatments in agroindustrial residues for the production of fungal glucanases and xylanases |
author |
Silva, D. F. [UNESP] |
author_facet |
Silva, D. F. [UNESP] Hergesel, L. M. [UNESP] Campioni, T. S. [UNESP] Carvalho, A. F.A. [UNESP] Oliva-Neto, P. [UNESP] |
author_role |
author |
author2 |
Hergesel, L. M. [UNESP] Campioni, T. S. [UNESP] Carvalho, A. F.A. [UNESP] Oliva-Neto, P. [UNESP] |
author2_role |
author author author author |
dc.contributor.none.fl_str_mv |
Universidade Estadual Paulista (Unesp) |
dc.contributor.author.fl_str_mv |
Silva, D. F. [UNESP] Hergesel, L. M. [UNESP] Campioni, T. S. [UNESP] Carvalho, A. F.A. [UNESP] Oliva-Neto, P. [UNESP] |
dc.subject.por.fl_str_mv |
Fibrolytic enzyme complex Shake-flask cultures Stirred tank bioreactor Submerged fermentation (SmF) Trichoderma reesei QM9414 |
topic |
Fibrolytic enzyme complex Shake-flask cultures Stirred tank bioreactor Submerged fermentation (SmF) Trichoderma reesei QM9414 |
description |
The production and use of fibrolytic enzyme complex in the hydrolysis of lignocellulosic materials is an important strategy for renewable bioenergy. The different carbon sources (residues) with or without some pretreatments (biological or chemical) were analyzed in order to increase the production of fibrolytic enzyme. Glycosyl hydrolases and xylanases were produced using Trichoderma reesei QM9414. The influence of some crude or pre-treated agro-industrial residues as a carbon source was previously investigated using shake-flask cultures. Subsequently, the selection of the best culture medium was studied under different pH and temperature conditions in stirred tank bioreactor. Fibrolytic activities reached a maximum of 0.85 ± 0.07 FPU mL−1 (total cellulase), 3.14 ± 0.01 CMC mL−1 (endoglucanase) and 1.25 ± 0.14 U mL−1 (exoglucanase) with the orange peel residue; and 93.08 ± 3.27 U mL−1 (xylanase) with sugarcane bagasse under alkali pretreatment. In the stirred tank bioreactor the cellulolytic activity increased to 1.76 ± 0.00 FPU mL−1, about 2 times higher than in the shake-flasks or under studied conditions. The biosynthesis of the fibrolytic complex using agroindustrial residues supplemented was shown to reach a higher total cellulose production. |
publishDate |
2018 |
dc.date.none.fl_str_mv |
2018-12-11T17:18:03Z 2018-12-11T17:18:03Z 2018-04-01 |
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://dx.doi.org/10.1016/j.procbio.2018.02.008 Process Biochemistry, v. 67, p. 29-37. 1359-5113 http://hdl.handle.net/11449/175900 10.1016/j.procbio.2018.02.008 2-s2.0-85042156382 2-s2.0-85042156382.pdf |
url |
http://dx.doi.org/10.1016/j.procbio.2018.02.008 http://hdl.handle.net/11449/175900 |
identifier_str_mv |
Process Biochemistry, v. 67, p. 29-37. 1359-5113 10.1016/j.procbio.2018.02.008 2-s2.0-85042156382 2-s2.0-85042156382.pdf |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
Process Biochemistry 0,761 |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
29-37 application/pdf |
dc.source.none.fl_str_mv |
Scopus reponame:Repositório Institucional da UNESP instname:Universidade Estadual Paulista (UNESP) instacron:UNESP |
instname_str |
Universidade Estadual Paulista (UNESP) |
instacron_str |
UNESP |
institution |
UNESP |
reponame_str |
Repositório Institucional da UNESP |
collection |
Repositório Institucional da UNESP |
repository.name.fl_str_mv |
Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP) |
repository.mail.fl_str_mv |
|
_version_ |
1808128743774879744 |