Literature DB >> 33392800

Does the BioBLU 0.3f single-use scale to the BioFlo® 320 reuseable bioreactor on a matched volumetric oxygen mass transfer coefficient?

Williams Olughu1, Duncan Galbraith2, Cillian Paget2, Steve Ruscoe2, Josh Smith2, Alison Mason2.   

Abstract

The volumetric oxygen mass transfer coefficient ([Formula: see text]) is an essential parameter in aerobic high-cell density fermentation where the availability of oxygen to growing microorganisms is a limiting factor. Bioprocess teams looking to scale-up/down between the Eppendorf BioBLU 0.3f single-use vessel and the BioFlo® 320 reusable vessel bioreactors may find it challenging using a matched [Formula: see text]. The maximum [Formula: see text] of the BioFlo® 320 reusable bioreactor was 109 h-1, which was approximately twice that of the BioBLU 0.3f single-use vessel. The results here show no overlap in [Formula: see text] values when both bioreactors were compared and thus conclude that scalability based on [Formula: see text] is not viable. The maximum [Formula: see text] of the Eppendorf BioBLU 0.3f single-use reported here was 47 h-1 compared to that of the manufacturer's value of 2500 h-1, indicating a 53-fold difference. This discrepancy was attributed to the incompatible sulfite addition method used by the manufacturer for estimation.

Entities:  

Keywords:  Bioprocess development; Bioreactor characterization; Fermentation; Scale down of bioprocesses; Scale up of fermentation

Mesh:

Substances:

Year:  2021        PMID: 33392800      PMCID: PMC7779418          DOI: 10.1007/s11274-020-02968-2

Source DB:  PubMed          Journal:  World J Microbiol Biotechnol        ISSN: 0959-3993            Impact factor:   3.312


  3 in total

1.  Gas-liquid dispersion with dual Rushton turbine impellers.

Authors:  V Hudcova; V Machon; A W Nienow
Journal:  Biotechnol Bioeng       Date:  1989-08-20       Impact factor: 4.530

Review 2.  Problems in scale-up of biotechnology production processes.

Authors:  H B Reisman
Journal:  Crit Rev Biotechnol       Date:  1993       Impact factor: 8.429

3.  Scale-down studies for the scale-up of a recombinant Corynebacterium glutamicum fed-batch fermentation: loss of homogeneity leads to lower levels of cadaverine production.

Authors:  Williams Olughu; Alvin Nienow; Chris Hewitt; Chris Rielly
Journal:  J Chem Technol Biotechnol       Date:  2019-11-21       Impact factor: 3.174

  3 in total

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