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Continuous production of human leukocyte interferon withEscherichia coli and continuous cell lysis in a two stage chemostat

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Summary

The continuous production and extrac-tion of human leukocyte interferon (type α2) in a two stage chemostat is described. Interferon con-tainingEscherichia coli cells were produced in the first stage and transferred to the second stage, where the cells were lysed continuously by the ad-dition of ampicillin. The medium used was based on corn steep liquor. Highest interferon titres and the best extraction efficiencies were achieved when running the first and second stages at dilution rates of 0.3 h−1 and 0.1 h−1, and at temperatures of 30° C and 25 °C, respectively. In order to prevent loss of interferon in the second stage, oxygen limitation had to be avoided. For optimal cell lysis there should be excess glucose in the second stage and the ampicillin concentration should be maintained above 100 mg 1−1.

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References

  • Emerick AE, Bertolani BL, Ben-Basset A, White TJ, Konrad MW (1984) Expression of a β-lactamase preproinsulin fusion protein inEscherichia coli. Biotechnology 2:165–173

    Article  CAS  Google Scholar 

  • Finter NB (1969) Dye uptake methods of assessing viral cytopathogenicity and their application of interferon assays. J Gen Virol 5:419–425

    Article  CAS  Google Scholar 

  • Guerra-Santos L, Käppeli O, Fiechter A (1984)Pseudomonas aeruginosa biosurfactant production in continuous culture with glucose as carbon source. Appl Environ Microbiol 48:301–305

    CAS  Google Scholar 

  • Kuhn H, Friederich U, Fiechter A (1979) Defined minimal medium for a thermophilicBacillus sp. developed by a chemostat pulse and shift technique. Eur J Appl Microbiol Biotechnol 6:341–349

    Article  CAS  Google Scholar 

  • Meyer H-P, Kuhn H-J, Brown SW, Fiechter A (1984) Production of human leukocyte interferon byEscherichia coli. Proceedings of the 3rd European Congress on Biotechnology: Vol 1, 499–505

    CAS  Google Scholar 

  • Nagata S, Taira H, Hall A, Johnsrud L, Streuli M, Ecsoedi J, Ball W, Cantell K, Weissmann C (1980) Synthesis inE. coli of a polypeptide with human leukocyte interferon activity. Nature 284:316–320

    Article  CAS  Google Scholar 

  • Reiling H, Laurila H, Fiechter A (1985) Medium development for low and high density cultivation ofEscherichia coli B/R in minimal and complex media. J Biotechnol 2:191–206

    Article  CAS  Google Scholar 

  • Toda K, Takeuchi T, Sano H (1983) Growth rate dependence of enzyme synthesis in chemostat cultures: α-amylase, β-galactosidase and β-fructosidase. J Chem Tech Biotechnol 29:747–755

    Google Scholar 

  • Zabriskie DW, Arminger WB, Phillips DH, Albano PA (1980) Traders guide to fermentation media. Traders Oil Mill Co., Fort Worth, Texas 76101, USA

    Google Scholar 

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Brown, S.W., Meyer, HP. & Fiechter, A. Continuous production of human leukocyte interferon withEscherichia coli and continuous cell lysis in a two stage chemostat. Appl Microbiol Biotechnol 23, 5–9 (1985). https://doi.org/10.1007/BF02660110

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  • DOI: https://doi.org/10.1007/BF02660110

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