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Cell engineering of Escherichia coli allows high cell density accumulation without fed-batch process control

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Abstract

A set of mutations in the phosphoenolpyruvate:carbohydrate phosphotransferase system (PTS) was used to create Escherichia coli strains with a reduced uptake rate of glucose. This allows a growth restriction, which is controlled on cellular rather than reactor level, which is typical of the fed-batch cultivation concept. Batch growth of the engineered strains resulted in cell accumulation profiles corresponding to a growth rate of 0.78, 0.38 and 0.25 h−1, respectively. The performance of the mutants in batch cultivation was compared to fed-batch cultivation of the wild type cell using restricted glucose feed to arrive at the corresponding growth profiles. Results show that the acetate production, oxygen consumption and product formation were similar, when a recombinant product was induced from the lacUV5 promoter. Ten times more cells could be produced in batch cultivation using the mutants without the growth detrimental production of acetic acid. This allows high cell density production without the establishment of elaborate fed-batch control equipment. The technique is suggested as a versatile tool in high throughput multiparallel protein production but also for increasing the number of experiments performed during process development while keeping conditions similar to the large-scale fed-batch performance.

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Acknowledgments

This work was sponsored by the Swedish Centre for Bioprocess Technology, CBioPT, which is gratefully acknowledged. We thank the Lundberg laboratory at the University of Gothenburg (Prof. Thomas Nyström and Dr Anne Farewell) and the University of Amsterdam (Profs. Peter Postma and Joost Teixeira de Mattos) for kindly supplying the strains and plasmids used in this work which were constructed in a joint EU Framework IV project: BIO4-CT98-0167.

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Correspondence to Gen Larsson.

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Bäcklund, E., Markland, K. & Larsson, G. Cell engineering of Escherichia coli allows high cell density accumulation without fed-batch process control. Bioprocess Biosyst Eng 31, 11–20 (2008). https://doi.org/10.1007/s00449-007-0144-x

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  • DOI: https://doi.org/10.1007/s00449-007-0144-x

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