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Related Concept Videos

Fed-Batch Culture01:23

Fed-Batch Culture

Fed-batch culture is a widely used bioprocessing strategy combining aspects of batch culture with controlled substrate feeding to optimize cell growth and product formation. In this semi-closed system, nutrients are strategically added during fermentation, while the accumulated products and biomass remain within the bioreactor until the end of the operation. This controlled addition of substrates allows for better management of growth kinetics, nutrient limitation, and metabolite...
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Nutrient Regulation by Continuous Feeding for Large-scale Expansion of Mammalian Cells in Spheroids
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A simple substrate feeding strategy using a pH control trigger in fed-batch fermentation.

Tiong-Ee Ting1, Gregory J Thoma, Robert R Beitle

  • 1Ralph E. Martin Department of Chemical Engineering, University of Arkansas, 3202 Bell Engineering Center, Fayetteville, AR 72701, USA.

Applied Biochemistry and Biotechnology
|March 20, 2008
PubMed
Summary

This study introduces a simple pH-controlled glucose feeding method for high-cell-density fed-batch fermentation. This automated strategy effectively boosts biomass production in Escherichia coli without direct glucose monitoring.

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Area of Science:

  • Biotechnology
  • Microbial Fermentation
  • Process Control

Background:

  • High-cell-density fed-batch fermentation is crucial for producing biomass and metabolites.
  • Accurate control of nutrient feeding, especially glucose, is essential for optimizing fermentation processes.
  • Traditional methods often rely on direct glucose measurement, which can be complex and costly.

Purpose of the Study:

  • To develop a simple, automated glucose feeding strategy for fed-batch fermentation using pH control.
  • To demonstrate the effectiveness of this strategy for biomass production in Escherichia coli.
  • To evaluate the performance of the strategy with different pH controllers.

Main Methods:

  • Developed an automated glucose feeding strategy based on pH control, using acidified glucose solution.
  • Determined glucose addition frequency based on culture growth kinetics.
  • Conducted fed-batch fermentations with indigenous and recombinant Escherichia coli strains.
  • Compared a portable pH controller with a proportional-integral-derivative (PID) controller.

Main Results:

  • Achieved high biomass production (optical density > 40 at 600 nm) for both E. coli strains.
  • Successfully applied the pH-controlled glucose feeding strategy with both types of pH controllers.
  • Observed improved control performance with the more sophisticated PID controller.
  • Demonstrated effective indirect glucose control without online glucose measurement.

Conclusions:

  • A simple pH-based glucose feeding strategy can effectively achieve high-cell-density fed-batch fermentation.
  • This method is adaptable to conventional bioreactors and simplifies the process by eliminating the need for online glucose sensors.
  • The strategy shows promise for optimizing biomass and secondary metabolite production.