Application of a multiphase microreactor chemostat for the determination of reaction kinetics of Staphylococcus carnosus

Bioreactors at the microliter scale offer a promising approach to accelerate bioprocess development. Advantages of such microbioreactors include a reduction in the use of expensive reagents. In this study, a chemostat operation mode of a cuvette-based microbubble column bioreactor made of polystyren...

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Published inBioprocess and biosystems engineering Vol. 42; no. 6; pp. 953 - 961
Main Authors Maldonado, S. Lladó, Krull, J., Rasch, D., Panjan, P., Sesay, A. M., Marques, M. P. C., Szita, N., Krull, R.
Format Journal Article
LanguageEnglish
Published Berlin/Heidelberg Springer Berlin Heidelberg 01.06.2019
Springer Nature B.V
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Summary:Bioreactors at the microliter scale offer a promising approach to accelerate bioprocess development. Advantages of such microbioreactors include a reduction in the use of expensive reagents. In this study, a chemostat operation mode of a cuvette-based microbubble column bioreactor made of polystyrene (working volume of 550 µL) was demonstrated. Aeration occurs through a nozzle ( Ø  ≤ 100 µm) and supports submerged whole-cell cultivation of Staphylococcus carnosus . Stationary concentrations of biomass and glucose were determined in the dilution rate regime ranging from 0.12 to 0.80 1/h with a glucose feed concentration of 1 g/L. For the first time, reaction kinetics of S. carnosus were estimated from data obtained from continuous cultivation. The maximal specific growth rate ( µ max  = 0.824 1/h), Monod constant ( K S  = 34 × 10 − 3 g S /L), substrate-related biomass yield coefficient ( Y X/S  = 0.315 g CDW /g S ), and maintenance coefficient ( m S  = 0.0035 g S /(g CDW ·h)) were determined. These parameters are now available for further studies in the field of synthetic biology.
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ISSN:1615-7591
1615-7605
DOI:10.1007/s00449-019-02095-9