ArticleBiotechnology and bioengineering2017
Segmented linear modeling of CHO fed-batch culture and its application to large scale production.
Article in Biotechnology and bioengineering, 2017. The graph could read no effect estimate from its abstract, so it casts no vote on the map. Cited by 5 papers.
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5 citing papers in PubMed, 27 citations in OpenAlex.
- LLM-Guided Parameter Optimization for Mechanistic CHO Cell Bioreactor Models.Biotechnology and bioengineering · 2026Article
- Analysis of cell lysis for improved understanding between the shake tube and stirred tank reactor perfusion CHO cell cultures.Cytotechnology · 2025Article
- A novel approach for perfusion process design based on a "Grey-Box" kinetic model.Bioprocess and biosystems engineering · 2024Article
- Advancements in CHO metabolomics: techniques, current state and evolving methodologies.Frontiers in bioengineering and biotechnology · 2024Review
- Process Analytical Technology for Advanced Process Control in Biologics Manufacturing with the Aid of Macroscopic Kinetic Modeling.Bioengineering (Basel, Switzerland) · 2018Article
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Authors and funding
4 authors at 3 institutions in 3 countries.
Funding
No grant is acknowledged in the PubMed record.
Abstract
We describe a systematic approach to model CHO metabolism during biopharmaceutical production across a wide range of cell culture conditions. To this end, we applied the metabolic steady state concept. We analyzed and modeled the production rates of metabolites as a function of the specific growth rate. First, the total number of metabolic steady state phases and the location of the breakpoints were determined by recursive partitioning. For this, the smoothed derivative of the metabolic rates with respect to the growth rate were used followed by hierarchical clustering of the obtained partition. We then applied a piecewise regression to the metabolic rates with the previously determined number of phases. This allowed identifying the growth rates at which the cells underwent a metabolic shift. The resulting model with piecewise linear relationships between metabolic rates and the growth rate did well describe cellular metabolism in the fed-batch cultures. Using the model structure and parameter values from a small-scale cell culture (2 L) training dataset, it was possible to predict metabolic rates of new fed-batch cultures just using the experimental specific growth rates. Such prediction was successful both at the laboratory scale with 2 L bioreactors but also at the production scale of 2000 L. This type of modeling provides a flexible framework to set a solid foundation for metabolic flux analysis and mechanistic type of modeling. Biotechnol. Bioeng. 2017;114: 785-797. © 2016 The Authors. Biotechnology and Bioengineering Published by Wiley Periodicals, Inc.
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