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Updated: Nov 27, 2025

The Use of Chemostats in Microbial Systems Biology
Published on: October 14, 2013
From Physics to Bioengineering: Microbial Cultivation Process Design and Feeding Rate Control Based on Relative
Renaldas Urniezius1, Vytautas Galvanauskas1, Arnas Survyla1
1Department of Automation, Kaunas University of Technology, Kaunas LT-51367, Lithuania.
This study introduces a novel optimization method for fed-batch cultivation, enhancing control and reproducibility in bioprocesses. The new approach eliminates the need for glucose measurements, simplifying microbial cultivation.
Area of Science:
- Biotechnology
- Process Engineering
- Control Theory
Background:
- Industrial fed-batch cultivation traditionally relies on open-loop feeding control due to historical reasons, regulations, and the need for reproducibility.
- Existing methods often require continuous monitoring, such as glucose concentration measurements, for effective process management.
Purpose of the Study:
- To develop a numerical semi-global convex optimization procedure for calculating feeding rate time profiles in fed-batch cultivation.
- To enhance reproducibility, controllability, and process performance in industrial biotechnological processes.
- To create a method that reduces reliance on real-time measurements like glucose concentration.
Main Methods:
- Utilized a generic gray box biomass modeling procedure incorporating relative entropy as a key optimization metric.
- Introduced a multivariate path of Lagrange multipliers and a concept of nuisance time for posterior distribution approximation.
- Developed a numerical semi-global convex optimization algorithm for feeding rate profile calculation.
Main Results:
- The proposed optimization method, based on relative entropy, is applicable beyond specific gray box models and bioengineering contexts.
- The technique offers advantages for both feed-forward and adaptive control systems requiring biomass growth prediction models.
- Identified gray box model parameters enable exploration of alternatives in controllable industrial biotechnological processes.
- Demonstrated that glucose concentration measurements become unnecessary for process development post-model identification.
Conclusions:
- The developed numerical optimization procedure offers a robust and versatile tool for designing fed-batch cultivation processes.
- This approach significantly improves process control, reproducibility, and performance, while simplifying operational requirements.
- The method's independence from specific models and real-time measurements broadens its applicability in industrial biotechnology.
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