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Effect of impeller type on cellular morphology and production of clavulanic acid by Streptomyces clavuligerus.
Bustamante, M C C; Costa, C L L; Esperança, M N; Mazziero, V T; Cerri, M O; Badino, Alberto C.
Afiliación
  • Bustamante MCC; Department of Chemical Engineering, Federal University of São Carlos, C.P. 676, São Carlos, SP, 13565-905, Brazil.
  • Costa CLL; Department of Chemical Engineering, Federal University of São Carlos, C.P. 676, São Carlos, SP, 13565-905, Brazil.
  • Esperança MN; Federal Institute of Education, Science and Technology of São Paulo, Campus Capivari, Capivari, SP, 13360-000, Brazil.
  • Mazziero VT; Department of Bioprocesses Engineering and Biotechnology, Faculty of Pharmaceutical Sciences, São Paulo State University, Araraquara, SP, 14801-902, Brazil.
  • Cerri MO; Department of Bioprocesses Engineering and Biotechnology, Faculty of Pharmaceutical Sciences, São Paulo State University, Araraquara, SP, 14801-902, Brazil.
  • Badino AC; Department of Chemical Engineering, Federal University of São Carlos, C.P. 676, São Carlos, SP, 13565-905, Brazil. badinojr@ufscar.br.
Braz J Microbiol ; 55(2): 1167-1177, 2024 Jun.
Article en En | MEDLINE | ID: mdl-38557863
ABSTRACT
It is essential to evaluate the effects of operating conditions in submerged cultures of filamentous microorganisms. In particular, the impeller type influences the flow pattern, power consumption, and energy dissipation, leading to differences in the hydrodynamic environment that affect the morphology of the microorganism. This work investigated the effect of different impeller types, namely the Rushton turbine (RT-RT) and Elephant Ear impellers in up-pumping (EEUP) and down-pumping (EEDP) modes, on cellular morphology and clavulanic acid (CA) production by Streptomyces clavuligerus in a stirred-tank bioreactor. At 800 rpm and 0.5 vvm, the cultivations performed using RT-RT and EEUP impellers provided higher shear conditions and oxygen transfer rates than those observed with EEDP. These conditions resulted in higher clavulanic acid production using RT-RT (380.7 mg/L) and EEUP (453.3 mg/L) impellers, compared to EEDP (196.6 mg/L). Although the maximum CA concentration exhibited the same order of magnitude for RT-RT and EEUP impellers, the latter presented 40% of the specific power consumption (4.9 kW/m3) compared to the classical RT-RT (12.0 kW/m3). The specific energy for CA production ( E CA ), defined as the energy cost to produce 1 mg of CA, was 3.5 times lower using the EEUP impeller (1.91 kJ/mgCA) when compared to RT-RT (5.91 kJ/mgCA). Besides, the specific energy for O2 transfer ( E O 2 ), the energy required to transfer 1 mmol of O2, was 2.3 times lower comparing the EEUP impeller (3.28 kJ/mmolO2) to RT-RT (7.65 kJ/mmolO2). The results demonstrated the importance of choosing the most suitable impeller configuration in conventional bioreactors to manufacture bioproducts.
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Texto completo: 1 Colección: 01-internacional Base de datos: MEDLINE Asunto principal: Streptomyces / Reactores Biológicos / Ácido Clavulánico Idioma: En Revista: Braz J Microbiol Año: 2024 Tipo del documento: Article País de afiliación: Brasil Pais de publicación: Brasil
Texto completo
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Imprimir
XML
PubMed Links
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Texto completo: 1 Colección: 01-internacional Base de datos: MEDLINE Asunto principal: Streptomyces / Reactores Biológicos / Ácido Clavulánico Idioma: En Revista: Braz J Microbiol Año: 2024 Tipo del documento: Article País de afiliación: Brasil Pais de publicación: Brasil