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Influence of operational parameters on the start-up of a flocculation airlift bioreactor

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Summary:The evolution of the fermentation parameters of a flocculating Saccharomyces yeast strain started up in a continuously operated internal loop airlift bioreactor was compared at different aeration rates (0.02 and 0.1 v.v.m., where v.v.m. represents the volume of air per volume of fermenter per minute and has the units 11−1 min−1) and dilution rates (0.1 and 0.2 h−1). The floc size distributions obtained were found to be different. The operating parameters do not seem to affect the glucose consumption rates, but instead affect the stoichiometry of its conversion to either ethanol or biomass, suggesting a shift in the metabolic mechanisms as biomass builds up. Oxygen availability was not uniform in the fermenter, according to the global volumetric mass transfer coefficients determined. The subsequent results establish a strong influence of the dilution and aeration rates on the measured variables (glucose, ethanol and biomass concentrations) and the calculated kinetic parameters (specific rates of glucose consumption, ethanol production and biomass growth).
Main Authors:Sousa, M. Luísa
Other Authors:Mota, M.; Teixeira, J. A.
Subject:Airlift bioreactor Diffusion Flocculation Floc size Oxygen transfer Yeast
Year:1994
Country:Portugal
Document type:article
Access type:open access
Associated institution:Universidade do Minho
Language:English
Origin:RepositóriUM - Universidade do Minho
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author Sousa, M. Luísa
author2 Mota, M.
Teixeira, J. A.
author2_role author
author
author_facet Sousa, M. Luísa
Mota, M.
Teixeira, J. A.
author_role author
contributor_name_str_mv Universidade do Minho
country_str PT
creators_json_txt [{\"Person.name\":\"Sousa, M. Luísa\"},{\"Person.name\":\"Mota, M.\"},{\"Person.name\":\"Teixeira, J. A.\"}]
datacite.contributors.contributor.contributorName.fl_str_mv Universidade do Minho
datacite.creators.creator.creatorName.fl_str_mv Sousa, M. Luísa
Mota, M.
Teixeira, J. A.
datacite.date.Accepted.fl_str_mv 1994-01-01T00:00:00Z
datacite.date.available.fl_str_mv 2013-10-16T13:26:02Z
datacite.date.embargoed.fl_str_mv 2013-10-16T13:26:02Z
datacite.rights.fl_str_mv http://purl.org/coar/access_right/c_abf2
datacite.subjects.subject.fl_str_mv Airlift bioreactor
Diffusion
Flocculation
Floc size
Oxygen transfer
Yeast
datacite.titles.title.fl_str_mv Influence of operational parameters on the start-up of a flocculation airlift bioreactor
dc.contributor.none.fl_str_mv Universidade do Minho
dc.creator.none.fl_str_mv Sousa, M. Luísa
Mota, M.
Teixeira, J. A.
dc.date.Accepted.fl_str_mv 1994-01-01T00:00:00Z
dc.date.available.fl_str_mv 2013-10-16T13:26:02Z
dc.date.embargoed.fl_str_mv 2013-10-16T13:26:02Z
dc.format.none.fl_str_mv application/pdf
dc.identifier.none.fl_str_mv https://hdl.handle.net/1822/25736
dc.language.none.fl_str_mv eng
dc.publisher.none.fl_str_mv Elsevier
dc.rights.none.fl_str_mv http://purl.org/coar/access_right/c_abf2
dc.subject.none.fl_str_mv Airlift bioreactor
Diffusion
Flocculation
Floc size
Oxygen transfer
Yeast
dc.title.fl_str_mv Influence of operational parameters on the start-up of a flocculation airlift bioreactor
dc.type.none.fl_str_mv http://purl.org/coar/resource_type/c_6501
description The evolution of the fermentation parameters of a flocculating Saccharomyces yeast strain started up in a continuously operated internal loop airlift bioreactor was compared at different aeration rates (0.02 and 0.1 v.v.m., where v.v.m. represents the volume of air per volume of fermenter per minute and has the units 11−1 min−1) and dilution rates (0.1 and 0.2 h−1). The floc size distributions obtained were found to be different. The operating parameters do not seem to affect the glucose consumption rates, but instead affect the stoichiometry of its conversion to either ethanol or biomass, suggesting a shift in the metabolic mechanisms as biomass builds up. Oxygen availability was not uniform in the fermenter, according to the global volumetric mass transfer coefficients determined. The subsequent results establish a strong influence of the dilution and aeration rates on the measured variables (glucose, ethanol and biomass concentrations) and the calculated kinetic parameters (specific rates of glucose consumption, ethanol production and biomass growth).
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eu_rights_str_mv openAccess
format article
fulltext.url.fl_str_mv https://prod-dspace.uminho.pt/bitstreams/a0655533-f5cf-4607-86dc-a6ecdea65250/download
id rum_c0d8a99d93216dcc892caec2664aea1e
identifier.url.fl_str_mv https://hdl.handle.net/1822/25736
instacron_str repositorium
institution Universidade do Minho
instname_str Universidade do Minho
language eng
network_acronym_str rum
network_name_str RepositóriUM - Universidade do Minho
oai_identifier_str oai:repositorium.uminho.pt:1822/25736
organization_str_mv urn:organizationAcronym:repositorium
person_str_mv Sousa, M. Luísa
Mota, M.
Teixeira, J. A.
publishDate 1994
publisher.none.fl_str_mv Elsevier
reponame_str RepositóriUM - Universidade do Minho
repository_id_str urn:repositoryAcronym:rum
service_str_mv urn:repositoryAcronym:rum
spelling engElsevierporThe evolution of the fermentation parameters of a flocculating Saccharomyces yeast strain started up in a continuously operated internal loop airlift bioreactor was compared at different aeration rates (0.02 and 0.1 v.v.m., where v.v.m. represents the volume of air per volume of fermenter per minute and has the units 11−1 min−1) and dilution rates (0.1 and 0.2 h−1). The floc size distributions obtained were found to be different. The operating parameters do not seem to affect the glucose consumption rates, but instead affect the stoichiometry of its conversion to either ethanol or biomass, suggesting a shift in the metabolic mechanisms as biomass builds up. Oxygen availability was not uniform in the fermenter, according to the global volumetric mass transfer coefficients determined. The subsequent results establish a strong influence of the dilution and aeration rates on the measured variables (glucose, ethanol and biomass concentrations) and the calculated kinetic parameters (specific rates of glucose consumption, ethanol production and biomass growth).application/pdfporInfluence of operational parameters on the start-up of a flocculation airlift bioreactorSousa, M. LuísaMota, M.Teixeira, J. A.HostingInstitutionOrganizationalUniversidade do Minhoe-mailmailto:repositorium@usdb.uminho.ptrepositorium@usdb.uminho.ptISSNIsPartOf0927-7765DOIIsPartOf10.1016/0927-7765(94)80033-22013-10-16T13:26:02Z19941994-01-01T00:00:00ZHandlehttps://hdl.handle.net/1822/25736http://purl.org/coar/access_right/c_abf2open accessAirlift bioreactorDiffusionFlocculationFloc sizeOxygen transferYeast871835 bytesliteraturehttp://purl.org/coar/resource_type/c_6501journal articlehttp://purl.org/coar/access_right/c_abf2application/pdffulltexthttps://prod-dspace.uminho.pt/bitstreams/a0655533-f5cf-4607-86dc-a6ecdea65250/download
spellingShingle Influence of operational parameters on the start-up of a flocculation airlift bioreactor
Sousa, M. Luísa
Airlift bioreactor
Diffusion
Flocculation
Floc size
Oxygen transfer
Yeast
status SINGLETON
subject.fl_str_mv Airlift bioreactor
Diffusion
Flocculation
Floc size
Oxygen transfer
Yeast
title Influence of operational parameters on the start-up of a flocculation airlift bioreactor
title_full Influence of operational parameters on the start-up of a flocculation airlift bioreactor
title_fullStr Influence of operational parameters on the start-up of a flocculation airlift bioreactor
title_full_unstemmed Influence of operational parameters on the start-up of a flocculation airlift bioreactor
title_short Influence of operational parameters on the start-up of a flocculation airlift bioreactor
title_sort Influence of operational parameters on the start-up of a flocculation airlift bioreactor
topic Airlift bioreactor
Diffusion
Flocculation
Floc size
Oxygen transfer
Yeast
topic_facet Airlift bioreactor
Diffusion
Flocculation
Floc size
Oxygen transfer
Yeast
url https://hdl.handle.net/1822/25736
visible 1