Abstract
Objectives
Development of an open-loop fed-batch protocol for highly reproducible fermentation of fission yeast that starts from batch cultures instead of glucose-limited aerobic chemostat cultures.
Results
A new strategy was employed that consists of an exponential feeding phase followed by a starvation period and then a linear feeding phase. A comparison of several independent fed-batch fermentations of a recombinant fission yeast strain showed that while during the initial phase process parameters such as glucose consumption and CO2 evolution varied considerably as expected, they were much more uniform during the third phase. For instance, the normalized standard deviation of glucose consumption was thirty times higher during the exponential feeding phase of the fermentation that during the linear feeding phase.
Conclusion
These data demonstrate the usefulness of the proposed strategy. It is expected that by variation of only two parameters (the total amount of glucose fed in the initial phase and the time frame of the starvation phase) the protocol can easily be adapted to other microbes.
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Supporting informations
Supplementary Fig. 1—Comparison of continuous carbon dioxide evolution (CO2%; bottom) and dissolved oxygen (DO %; top) measurements during three individual fed-batch cultivations of strain JMN8. Each color (purple, orange, magenta) represents the measurements of an individual fermentation run.
Supplementary Fig. 2—Fed-batch cultivation of strain CAD75 at pH 5.5. Total glucose fed (brown) was calculated continuously; samples were taken periodically and analyzed for glucose concentration (red) and biomass (blue) as indicated. Glucose consumption rates during different time intervals are shown in light purple.
Supplementary Fig. 3—Comparison of continuous carbon dioxide evolution (CO2 (%); bottom) and dissolved oxygen (DO; top) measurements during fed-batch cultivation of strain CAD75 at pH 5.5 (top row) and CO2 evolution rates (d([CO2])/dt; bottom row). The CO2 evolution rates are the first-order derivatives of the CO2 evolution profiles shown in the top row. The markings correspond to the respective regions in the CO2 evolution profiles.
Supplementary Fig. 4—Fed-batch cultivation of strain CAD75 at pH 3. Total glucose fed (brown) was calculated continuously; samples were taken periodically and analyzed for glucose concentration (red) and biomass (blue) as indicated. Glucose consumption rates during different time intervals are shown in light purple.
Supplementary Fig. 5—Comparison of continuous carbon dioxide evolution (CO2 (%); bottom) and dissolved oxygen (DO; top) measurements during fed-batch cultivation of strain CAD75 at pH 3 (top row) and CO2 evolution rates (d([CO2])/dt; bottom row). The CO2 evolution rates are the first-order derivatives of the CO2 evolution profiles shown in the top row. The markings correspond to the respective regions in the CO2 evolution profiles.
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Scomparin, A., Bureik, M. A convenient new method for reproducible fed-batch fermentation of fission yeast Schizosaccharomyces pombe. Biotechnol Lett 42, 937–943 (2020). https://doi.org/10.1007/s10529-020-02840-1
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DOI: https://doi.org/10.1007/s10529-020-02840-1