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ORIGINAL RESEARCH article

Front. Bioeng. Biotechnol.
Sec. Bioprocess Engineering
Volume 12 - 2024 | doi: 10.3389/fbioe.2024.1479633

Cell Clone Selection -Impact of Operation Modes and Medium Exchange Strategies on Clone Ranking

Provisionally accepted
Marie Dorn Marie Dorn 1Christine Ferng Christine Ferng 2Kerensa Klottrup-Rees Kerensa Klottrup-Rees 3*Kenneth Lee Kenneth Lee 2*Martina Micheletti Martina Micheletti 1*
  • 1 The Advanced Centre for Biochemical Engineering, Department of Biochemical Engineering, Faculty of Engineering Sciences, University College London, London, United Kingdom
  • 2 BioProcess Technologies and Engineering, Biopharmaceutical Developments, AstraZeneca, Gaithersburg, United States
  • 3 Cell Culture and Fermentation Sciences, Biopharmaceutical Development, AstraZeneca, Cambridge, United Kingdom

The final, formatted version of the article will be published soon.

    Bioprocessing has been transitioning from batch to continuous processes. As a result, a considerable amount of resource was dedicated to optimising strategies for continuous processes. However, the focus has been on developing a suitable and scalable perfusion strategy with little attention given to the selection of optimal cell clones.Cell line development and lead clone selection are critical to bioprocess development. The screening and selection process is typically performed in stages. Microwell plates (MWP) are used to narrow down the number of clone candidates, which will undergo further selective screening in progressively larger small-scale bioreactors (12 mL -3L) to identify the top clone for GMP production. Perfusion mode of operation is typically applied at bench-scale for optimisation purposes, while process development and cell clone screening studies at mL-scale still commonly use fed-batch methods. The change of operation mode from bolus feeding to perfusion with a regular exchange of medium, leads to questions regarding the reliability and fit of initial clone selection. Is the early-stage clone ranking impacted by the discrepancy in the operation mode, and does this potentially result in the exclusion of cell clones suitable for perfusion processes?To address this question, we evaluated various CHO cell clones expressing two antibody products using MWP methodologies in fed-batch and semi-perfusion mode. We assessed growth, metabolic, and productivity performance, and ranked cell clones using two different strategies. The first strategy evaluated clones based on a single parameter: the cell-specific productivity (qP). The second considered a collection of multiple parameters using the metric of the Manufacturability index (MICL).Both ranking strategies showed an impact of operation mode and perfusion rate on the clone ranking.Notably, depending on the chosen operation mode, different sets of candidate clones might have been selected for further, more extensive screening. Additionally, we evaluated the reproducibility of our results demonstrating consistency in cell clone growth performance and ranking.

    Keywords: Perfusion, Fed-batch, Small-scale, Microwell plate, high-throughput, cell clone screening, cell clone ranking

    Received: 12 Aug 2024; Accepted: 19 Dec 2024.

    Copyright: © 2024 Dorn, Ferng, Klottrup-Rees, Lee and Micheletti. This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) or licensor are credited and that the original publication in this journal is cited, in accordance with accepted academic practice. No use, distribution or reproduction is permitted which does not comply with these terms.

    * Correspondence:
    Kerensa Klottrup-Rees, Cell Culture and Fermentation Sciences, Biopharmaceutical Development, AstraZeneca, Cambridge, United Kingdom
    Kenneth Lee, BioProcess Technologies and Engineering, Biopharmaceutical Developments, AstraZeneca, Gaithersburg, United States
    Martina Micheletti, The Advanced Centre for Biochemical Engineering, Department of Biochemical Engineering, Faculty of Engineering Sciences, University College London, London, United Kingdom

    Disclaimer: All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors and the reviewers. Any product that may be evaluated in this article or claim that may be made by its manufacturer is not guaranteed or endorsed by the publisher.