Publicação:
Cephalosporin C production by immobilized Cephalosporium acremonium cells in a repeated batch tower bioreactor

dc.contributor.authorCruz, AJG
dc.contributor.authorPan, T.
dc.contributor.authorGiordano, R. C.
dc.contributor.authorAraujo, MLGC
dc.contributor.authorHokka, C. O.
dc.contributor.institutionUniversidade Federal de São Carlos (UFSCar)
dc.contributor.institutionUniversidade Estadual Paulista (Unesp)
dc.date.accessioned2014-05-20T15:25:42Z
dc.date.available2014-05-20T15:25:42Z
dc.date.issued2004-01-05
dc.description.abstractThe industrial production of antibiotics with filamentous fungi is usually carried out in conventional aerated and agitated tank fermentors. Highly viscous non-Newtonian broths are produced and a compromise must be found between convenient shear stress and adequate oxygen transfer. In this work, cephalosporin C production by bioparticles of immobilized cells of Cephalosporium acremonium ATCC 48272 was studied in a repeated batch tower bioreactor as an alternative to the conventional process. Also, gas-liquid oxygen transfer volumetric coefficients, k(L)a, were determined at various air flow-rates and alumina contents in the bioparticle. The bioparticles were composed of calcium alginate (2.0% w/w), alumina (<44 micra), cells, and water. A model describing the cell growth, cephalosporin C production, oxygen, glucose, and sucrose consumption was proposed. To describe the radial variation of oxygen concentration within the pellet, the reaction-diffusion model forecasting a dead core bioparticle was adopted. The k(L)a measurements with gel beads prepared with 0.0, 1.0, 1.5, and 2.0% alumina showed that a higher k(L)a value is attained with 1.5 and 2.0%. An expression relating this coefficient to particle density, liquid density, and air velocity was obtained and further utilized in the simulation of the proposed model. Batch, followed by repeated batch experiments, were accomplished by draining the spent medium, washing with saline solution, and pouring fresh medium into the bioreactor. Results showed that glucose is consumed very quickly, within 24 h, followed by sucrose consumption and cephalosporin C production. Higher productivities were attained during the second batch, as cell concentration was already high, resulting in rapid glucose consumption and an early derepression of cephalosporin C synthesizing enzymes. The model incorporated this improvement predicting higher cephalosporin C productivity. (C) 2004 Wiley Periodicals, Inc.en
dc.description.affiliationUniv Fed Sao Carlos, BR-13565905 Sao Carlos, SP, Brazil
dc.description.affiliationUniv Estadual Paulista, Dept Technol, Inst Quim, BR-14801970 Araraquara, SP, Brazil
dc.description.affiliationUnespUniv Estadual Paulista, Dept Technol, Inst Quim, BR-14801970 Araraquara, SP, Brazil
dc.format.extent96-102
dc.identifierhttp://dx.doi.org/10.1002/bit.10877
dc.identifier.citationBiotechnology and Bioengineering. Hoboken: John Wiley & Sons Inc., v. 85, n. 1, p. 96-102, 2004.
dc.identifier.doi10.1002/bit.10877
dc.identifier.issn0006-3592
dc.identifier.urihttp://hdl.handle.net/11449/36056
dc.identifier.wosWOS:000187634600010
dc.language.isoeng
dc.publisherWiley-Blackwell
dc.relation.ispartofBiotechnology and Bioengineering
dc.relation.ispartofjcr3.952
dc.relation.ispartofsjr1,372
dc.rights.accessRightsAcesso restrito
dc.sourceWeb of Science
dc.subjectcephalosporin C productionpt
dc.subjecttower bioreactorpt
dc.subjectrepeated-batchpt
dc.subjectimmobilized cellspt
dc.titleCephalosporin C production by immobilized Cephalosporium acremonium cells in a repeated batch tower bioreactoren
dc.typeArtigo
dcterms.licensehttp://olabout.wiley.com/WileyCDA/Section/id-406071.html
dcterms.rightsHolderWiley-Blackwell
dspace.entity.typePublication
unesp.author.orcid0000-0001-6830-9512[1]
unesp.author.orcid0000-0002-6679-0960[1]

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