Cellulose production by Gluconacetobacter kakiaceti GM5 in two batch process using vinasse as culture media
ABSTRACT: The present study was conducted to evaluate the cellulose production by Gluconacetobacter kakiaceti GM5 by means of two aerobic treatments: the static discontinuous fermentation process (treatment 1) and the discontinuous fermentation process in a rotary shaker (treatment 2). All these exp...
- Autores:
-
Fernández Calle, Erika Pamela
Velásquez Riaño, Möritz
Villa Restrepo, Andrés Felipe
Lombana Sánchez, Nelson
- Tipo de recurso:
- Article of investigation
- Fecha de publicación:
- 2015
- Institución:
- Universidad de Antioquia
- Repositorio:
- Repositorio UdeA
- Idioma:
- eng
- OAI Identifier:
- oai:bibliotecadigital.udea.edu.co:10495/31509
- Acceso en línea:
- https://hdl.handle.net/10495/31509
- Palabra clave:
- Fermentación
Fermentation
Aerobiosis
Celulosa - metabolismo
Cellulose - metabolism
Medios de Cultivo - química
Culture Media - chemistry
Gluconacetobacter - metabolismo
Gluconacetobacter - metabolism
- Rights
- openAccess
- License
- http://creativecommons.org/licenses/by-nc-nd/2.5/co/
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oai:bibliotecadigital.udea.edu.co:10495/31509 |
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UDEA2 |
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Repositorio UdeA |
repository_id_str |
|
dc.title.spa.fl_str_mv |
Cellulose production by Gluconacetobacter kakiaceti GM5 in two batch process using vinasse as culture media |
title |
Cellulose production by Gluconacetobacter kakiaceti GM5 in two batch process using vinasse as culture media |
spellingShingle |
Cellulose production by Gluconacetobacter kakiaceti GM5 in two batch process using vinasse as culture media Fermentación Fermentation Aerobiosis Celulosa - metabolismo Cellulose - metabolism Medios de Cultivo - química Culture Media - chemistry Gluconacetobacter - metabolismo Gluconacetobacter - metabolism |
title_short |
Cellulose production by Gluconacetobacter kakiaceti GM5 in two batch process using vinasse as culture media |
title_full |
Cellulose production by Gluconacetobacter kakiaceti GM5 in two batch process using vinasse as culture media |
title_fullStr |
Cellulose production by Gluconacetobacter kakiaceti GM5 in two batch process using vinasse as culture media |
title_full_unstemmed |
Cellulose production by Gluconacetobacter kakiaceti GM5 in two batch process using vinasse as culture media |
title_sort |
Cellulose production by Gluconacetobacter kakiaceti GM5 in two batch process using vinasse as culture media |
dc.creator.fl_str_mv |
Fernández Calle, Erika Pamela Velásquez Riaño, Möritz Villa Restrepo, Andrés Felipe Lombana Sánchez, Nelson |
dc.contributor.author.none.fl_str_mv |
Fernández Calle, Erika Pamela Velásquez Riaño, Möritz Villa Restrepo, Andrés Felipe Lombana Sánchez, Nelson |
dc.subject.decs.none.fl_str_mv |
Fermentación Fermentation Aerobiosis Celulosa - metabolismo Cellulose - metabolism Medios de Cultivo - química Culture Media - chemistry Gluconacetobacter - metabolismo Gluconacetobacter - metabolism |
topic |
Fermentación Fermentation Aerobiosis Celulosa - metabolismo Cellulose - metabolism Medios de Cultivo - química Culture Media - chemistry Gluconacetobacter - metabolismo Gluconacetobacter - metabolism |
description |
ABSTRACT: The present study was conducted to evaluate the cellulose production by Gluconacetobacter kakiaceti GM5 by means of two aerobic treatments: the static discontinuous fermentation process (treatment 1) and the discontinuous fermentation process in a rotary shaker (treatment 2). All these experiments were carried out using vinasse as experimental culture media (VM) and were compared with standard media containing glucose at 2% (standard medium (SM)). A sample of each treatment was extracted every 24 h over a period of 168 h. The maximum rates of cellulose produced in treatment 1 using SM added up to 3.63 ± 0.18 g l 1, and to 4.15 ± 0.16 g l 1 when VM was used. The amount of cellulose produced in treatment 2 using SM was 2.95 ± 0.09 g l 1 (which suggests an increase of 37%), and added up to 1.84 ± 0.07 g l 1 when using VM. A better global yield of both treatments in terms of sugar consumption after 168 h was obtained when using VM: 32% in treatment 1, whereas in treatment 2 it was 9%. A 20% decrease on vinasse COD (Chemical Oxy |
publishDate |
2015 |
dc.date.issued.none.fl_str_mv |
2015 |
dc.date.accessioned.none.fl_str_mv |
2022-10-27T20:09:39Z |
dc.date.available.none.fl_str_mv |
2022-10-27T20:09:39Z |
dc.type.spa.fl_str_mv |
info:eu-repo/semantics/article |
dc.type.coarversion.fl_str_mv |
http://purl.org/coar/version/c_970fb48d4fbd8a85 |
dc.type.hasversion.spa.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
dc.type.coar.spa.fl_str_mv |
http://purl.org/coar/resource_type/c_2df8fbb1 |
dc.type.redcol.spa.fl_str_mv |
https://purl.org/redcol/resource_type/ART |
dc.type.local.spa.fl_str_mv |
Artículo de investigación |
format |
http://purl.org/coar/resource_type/c_2df8fbb1 |
status_str |
publishedVersion |
dc.identifier.issn.none.fl_str_mv |
1606-9749 |
dc.identifier.uri.none.fl_str_mv |
https://hdl.handle.net/10495/31509 |
dc.identifier.doi.none.fl_str_mv |
10.2166/wst.2013.347 |
dc.identifier.eissn.none.fl_str_mv |
1607-0798 |
identifier_str_mv |
1606-9749 10.2166/wst.2013.347 1607-0798 |
url |
https://hdl.handle.net/10495/31509 |
dc.language.iso.spa.fl_str_mv |
eng |
language |
eng |
dc.relation.ispartofjournalabbrev.spa.fl_str_mv |
Water. Sci. Technol. Water. Supply. |
dc.rights.spa.fl_str_mv |
info:eu-repo/semantics/openAccess |
dc.rights.uri.*.fl_str_mv |
http://creativecommons.org/licenses/by-nc-nd/2.5/co/ |
dc.rights.accessrights.spa.fl_str_mv |
http://purl.org/coar/access_right/c_abf2 |
dc.rights.creativecommons.spa.fl_str_mv |
https://creativecommons.org/licenses/by-nc-nd/4.0/ |
eu_rights_str_mv |
openAccess |
rights_invalid_str_mv |
http://creativecommons.org/licenses/by-nc-nd/2.5/co/ http://purl.org/coar/access_right/c_abf2 https://creativecommons.org/licenses/by-nc-nd/4.0/ |
dc.format.extent.spa.fl_str_mv |
7 |
dc.format.mimetype.spa.fl_str_mv |
application/pdf |
dc.publisher.spa.fl_str_mv |
IWA Publishing |
dc.publisher.group.spa.fl_str_mv |
BIOMICRO Grupo de Biotransformación |
dc.publisher.place.spa.fl_str_mv |
Colchester, Inglaterra |
institution |
Universidad de Antioquia |
bitstream.url.fl_str_mv |
https://bibliotecadigital.udea.edu.co/bitstream/10495/31509/4/FernandezErika_2013_ProductionByGluconacetobacter.pdf https://bibliotecadigital.udea.edu.co/bitstream/10495/31509/2/license_rdf https://bibliotecadigital.udea.edu.co/bitstream/10495/31509/3/license.txt |
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94998662f530854534f8e4475b50bbc6 b88b088d9957e670ce3b3fbe2eedbc13 8a4605be74aa9ea9d79846c1fba20a33 |
bitstream.checksumAlgorithm.fl_str_mv |
MD5 MD5 MD5 |
repository.name.fl_str_mv |
Repositorio Institucional Universidad de Antioquia |
repository.mail.fl_str_mv |
andres.perez@udea.edu.co |
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1812173233769676800 |
spelling |
Fernández Calle, Erika PamelaVelásquez Riaño, MöritzVilla Restrepo, Andrés FelipeLombana Sánchez, Nelson2022-10-27T20:09:39Z2022-10-27T20:09:39Z20151606-9749https://hdl.handle.net/10495/3150910.2166/wst.2013.3471607-0798ABSTRACT: The present study was conducted to evaluate the cellulose production by Gluconacetobacter kakiaceti GM5 by means of two aerobic treatments: the static discontinuous fermentation process (treatment 1) and the discontinuous fermentation process in a rotary shaker (treatment 2). All these experiments were carried out using vinasse as experimental culture media (VM) and were compared with standard media containing glucose at 2% (standard medium (SM)). A sample of each treatment was extracted every 24 h over a period of 168 h. The maximum rates of cellulose produced in treatment 1 using SM added up to 3.63 ± 0.18 g l 1, and to 4.15 ± 0.16 g l 1 when VM was used. The amount of cellulose produced in treatment 2 using SM was 2.95 ± 0.09 g l 1 (which suggests an increase of 37%), and added up to 1.84 ± 0.07 g l 1 when using VM. A better global yield of both treatments in terms of sugar consumption after 168 h was obtained when using VM: 32% in treatment 1, whereas in treatment 2 it was 9%. A 20% decrease on vinasse COD (Chemical OxyCOL0111863COL00669917application/pdfengIWA PublishingBIOMICROGrupo de BiotransformaciónColchester, Inglaterrainfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articlehttp://purl.org/coar/resource_type/c_2df8fbb1https://purl.org/redcol/resource_type/ARTArtículo de investigaciónhttp://purl.org/coar/version/c_970fb48d4fbd8a85info:eu-repo/semantics/openAccesshttp://creativecommons.org/licenses/by-nc-nd/2.5/co/http://purl.org/coar/access_right/c_abf2https://creativecommons.org/licenses/by-nc-nd/4.0/Cellulose production by Gluconacetobacter kakiaceti GM5 in two batch process using vinasse as culture mediaFermentaciónFermentationAerobiosisCelulosa - metabolismoCellulose - metabolismMedios de Cultivo - químicaCulture Media - chemistryGluconacetobacter - metabolismoGluconacetobacter - metabolismWater. Sci. Technol. Water. Supply.Water Science & Technology: Water Supply10791084685ORIGINALFernandezErika_2013_ProductionByGluconacetobacter.pdfFernandezErika_2013_ProductionByGluconacetobacter.pdfArtículo de investigaciónapplication/pdf206515https://bibliotecadigital.udea.edu.co/bitstream/10495/31509/4/FernandezErika_2013_ProductionByGluconacetobacter.pdf94998662f530854534f8e4475b50bbc6MD54CC-LICENSElicense_rdflicense_rdfapplication/rdf+xml; charset=utf-8823https://bibliotecadigital.udea.edu.co/bitstream/10495/31509/2/license_rdfb88b088d9957e670ce3b3fbe2eedbc13MD52LICENSElicense.txtlicense.txttext/plain; charset=utf-81748https://bibliotecadigital.udea.edu.co/bitstream/10495/31509/3/license.txt8a4605be74aa9ea9d79846c1fba20a33MD5310495/31509oai:bibliotecadigital.udea.edu.co:10495/315092022-10-27 15:10:27.492Repositorio Institucional Universidad de Antioquiaandres.perez@udea.edu.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 |