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Discrimination of riboflavin producing Bacillus subtilis strains based on their fed-batch process performances on a millilitre scale

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Abstract

Forty-eight single-use stirred tank bioreactors on a 10-mL scale operated in a magnetically inductive driven bioreaction block and automated with a liquid handler were applied for discrimination of different riboflavin producing Bacillus subtilis strains based on their performances in the parallel fed-batch processes. It was shown that a discrimination of the B. subtilis riboflavin producer strains can efficiently be achieved within one parallel fermentation run based on the integral riboflavin yield after 48 h. The possibility to perform replicates within the parallel fermentation run allows for a robust statistical analysis and is a prerequisite for the discrimination of producer strains under fed-batch process conditions. Within the estimation error, all of the riboflavin producing B. subtilis strains under study showed the same fed-batch process performances on the litre scale compared to the millilitre scale.

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References

  • Betts J, Doig S, Baganz F (2006) Characterization and application of a miniature 10 mL stirred-tank bioreactor, showing scale-down equivalence with a conventional 7 L reactor. Biotechnol Prog 22:681–688

    Article  CAS  Google Scholar 

  • Harms P, Kostov Y, French J, Soliman M, Anjanappa M, Ram A, Rao G (2006) Design and performance of a 24-station high throughput microbioreactor. Biotechnol Bioeng 93:6–13

    Article  CAS  Google Scholar 

  • Hümbelin M, Griesser V, Keller T, Schurter W, Haiker M, Hohmann H-P, Ritz H, Richter G, Bacher A, van Loon APGM (1999) GTP cyclohydrolase II and 3, 4-dihydroxy-2-butanone 4-phosphate synthase are rate-limiting enzymes in riboflavin synthesis of an industrial Bacillus subtilis strain used for riboflavin production. J Indust Microbiol Biotechnol 22:1–7

    Article  Google Scholar 

  • Knorr B, Schlieker H, Hohmann H-P, Weuster-Botz D (2007) Scale-down and parallel operation of the riboflavin production process with Bacillus subtilis. Biochem Eng J 33:263–274

    Article  CAS  Google Scholar 

  • Kostov Y, Harms P, Randers-Eichhorn L, Rao G (2001) Low-cost microbioreactor for high-throughput bioprocessing. Biotechnol Bioeng 72:346–352

    Article  CAS  Google Scholar 

  • Kusterer A, Krause C, Kaufmann K, Arnold M, Weuster-Botz D (2008) Fully automated single-use stirred-tank bioreactors for parallel microbial cultivations. Bioproc Biosyst Eng 31:207–215

    Article  CAS  Google Scholar 

  • Lamping SR, Zhang H, Allen B, Shamlou PA (2003) Design of a prototype miniature bioreactor for high throughput automated bioprocessing. Chem Eng Sci 58:747–758

    Article  CAS  Google Scholar 

  • Lehmann M (2007): Modified transketolase and use thereof. European patent number WO 2007/051552 A1).

  • Link H, Weuster-Botz D (2006) Genetic algorithm for multi-objective experimental optimization. Bioproc Biosyst Eng 29:385–390

    Article  CAS  Google Scholar 

  • Perkins J, Sloma A, Hermann T, Thieriault K, Zachgo E, Erdenberger T, Hannet N, Chatterjee N, Williams V, Rufo G, Hatch R, Pero J (1999) Genetic engineering of Bacillus subtilis for the commercial production of riboflavin. J Indust Microbiol Biotechnol 22:8–12

    Article  CAS  Google Scholar 

  • Puskeiler R, Kaufmann K, Weuster-Botz D (2005a) Development, parallelization and automation of a gas-inducing milliliter-scale bioreactor for high-throughput bioprocess design (HTBD). Biotechnol Bioeng 89:512–523

    Article  CAS  Google Scholar 

  • Puskeiler R, Kusterer A, John G, Weuster-Botz D (2005b) Miniature bioreactors for automated high-throughput bioprocess design (HTBD): Reproducibility of parallel fed-batch cultivations with Escherichia coli. Biotechnol Appl Biochem 42:227–235

    Article  CAS  Google Scholar 

  • Rudolf M, Kulisch W (2008) Biostatistik. Pearson Studium, München

    Google Scholar 

  • Vallejos J, Kostov Y, Ram A, French J, Marten M, Rao G (2006) Optical analysis of liquid mixing in a minibioreactor. Biotechnol Bioeng 93:906–911

    Article  CAS  Google Scholar 

  • Weuster-Botz D, Puskeiler R, Kusterer A, Kaufmann K, John G, Arnold M (2005) Methods and milliliter scale devices for high-throughput bioprocess design. Bioproc Biosyst Eng 28:109–119

    Article  CAS  Google Scholar 

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Acknowledgements

The authors gratefully acknowledge the technical assistance of Eva Chervenkova, Fei Xue and Katharina Kinast in the labs at the Technische Universität München and the funding of the research work by DSM Nutritional Products, Basel, Switzerland.

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Correspondence to Dirk Weuster-Botz.

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Vester, A., Hans, M., Hohmann, HP. et al. Discrimination of riboflavin producing Bacillus subtilis strains based on their fed-batch process performances on a millilitre scale. Appl Microbiol Biotechnol 84, 71–76 (2009). https://doi.org/10.1007/s00253-009-1966-z

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  • DOI: https://doi.org/10.1007/s00253-009-1966-z

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