(541a) Model-Based Investigation of Upstream CHO Cell Culture Process for Production of Monoclonal Antibodies with Desired N-Linked Glycosylation | AIChE

(541a) Model-Based Investigation of Upstream CHO Cell Culture Process for Production of Monoclonal Antibodies with Desired N-Linked Glycosylation

Authors 

Venkatarama Reddy, J. - Presenter, University of Delaware
Yang, O. - Presenter, Rutgers, the State University of New Jersey
Raudenbush, K. - Presenter, University of Delaware
Chundawat, S., Rutgers University
Ierapetritou, M., University of Delaware
Gyorgypal, A., Rutgers University
N-linked glycosylation is post-translational protein modification that takes place during synthesis of monoclonal antibodies (mAbs) 1. N-linked glycan composition or glycan index, including total afucosylation, high mannosylation, fucosylation, and/or galactosylation indexes, are often critical quality attributes (CQAs) of mAb based therapeutic proteins 2. Researchers have found controlling the cell culture media components such as uridine, galactose, manganese, and ammonia concentration can tweak the glycosylation composition with the desired CQA levels 3-5. During bioreactor operations, many process parameters or operating conditions can also affect protein glycosylation such as temperature, pH and dissolved oxygen 6-8. However, the effect of process parameters on mAb glycosylation can vary significantly between different cell lines. To better understand the protein glycosylation process and further optimize the bioreactor operations, process modeling can be used to support quality by design (QbD) by correlating critical process parameters with critical quality attributes and further defining a design space for process operations.

We have investigated the effect of temperature and pH on protein glycosylation for a model Herceptin biosimilar (or Trastuzumab) production using a CHO cell culture cultivation in an upstream fed-batch bioreactor. Mechanistic kinetic model was developed based on the experimental data obtained under different temperature and pH combinations. The mechanistic model contains two parts, including an unstructured cell culture model and a structured intracellular model. For our unstructured cell culture model, viable cell density, glucose, ammonia, and protein concentrations are captured by empirical equations. In the structured model, the intracellular kinetics of biochemical reactions cascade of the N-linked glycosylation process are simulated. The kinetic model is used to understand the effect of temperature and pH on the bioprocess. Finally, feasibility analysis with surrogate-based adaptive sampling is applied to determine a bioreactor operation design space. In this combined experimental and computational study, we have determined how adjusting the bioreactor operating conditions can achieve critical quality attributes of the targeted product. Ongoing work will implement integration with a control system to achieve real-time process control for mAb glycosylation.

References

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