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Consejo Nacional de Ciencia y Tecnología, CONACYT: 33973-B
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World Journal of Microbiology and Biotechnology
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publication venue for: Mathematical description of bikaverin production in a fluidized bed bioreactor
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RDF description of Mathematical description of bikaverin production in a fluidized bed bioreactor - http://orbis.uaslp.mx/vivo/individual/scopus1490
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date: 2026-08-26T03:56:56
publisher: vivo
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Article
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Mathematical description of bikaverin production in a fluidized bed bioreactor
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page end: 688
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issue: 5
origen: scopus
crisid: 1491
doi: 10.1007/s11274-004-3854-0
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related by: authorship 9002
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has publication venue: World Journal of Microbiology and Biotechnology
related by: authorship 9000
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page start: 683
freetext keyword: Bikaverin; Fluidized bioreactor; Gibberella fujikuroi; Immobilized; Mathematical model Agglomeration; Biomass; Fermentation; Fluidized beds; Glucose; Mathematical models; Micelles; Reaction kinetics; Bikaverin production; Fluidized bed bioreactors; Gompertz model; Growth fitting; Bioreactors; Fungi; Gibberella fujikuroi
date time value: article date 1491
e iscopus: 2-s2.0-23144435793
related by: authorship 9003
abstract: Growth of Gibberella fujikuroi in submerged cultures occurs as micelles or filamentous hyphae dispersed in fluid and pellets or stable, spherical agglomerations. Gibberella fujikuroi growth, substrate consumption and bikaverin production kinetics obtained from submerged batch fermentation were fitted to three different sigmoid models: two and three-parameter Gompertz models and one Logistic model. Growth fitting was used to compare between models and select the best one by means of an F test. The best model for describing growth was the two-parameter Gompertz model and was used for glucose consumption and bikaverin production fitting. Data from eight different schemes of fermentations were analysed and parameter estimation was carried out by means of minimization of residual sum of squares. Some characteristic values obtained with the two-parameter Gompertz model fit are: μ=0.028 h-1, Y x/s =0.1089 g substrate/g biomass, α =0.1384 g product/g biomass. © Springer 2005.
volume: 21
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