A comprehensive study of glucose and oxygen gradients in a scaled-down model of recombinant HuGM-CSF production in thermoinduced fed-batch cultures.

Prep Biochem Biotechnol

Departamento de Biología Molecular y Biotecnología, Instituto de Investigaciones Biomédicas, Universidad Nacional Autónoma de México, Cd. Universitaria, Coyoacán, Ciudad de México, México.

Published: November 2024

AI Article Synopsis

  • The study investigates how elevated glucose and low oxygen levels affect cell growth and protein production in fed-batch bioreactor systems using two-compartment models.
  • When comparing the results from a plug flow bioreactor (PFB) connected to a stirred tank bioreactor (STB), cell growth was significantly diminished with increased residence times in the PFB.
  • The production of recombinant proteins, specifically rHuGM-CSF, also decreased with longer residence times, indicating metabolic shifts and potential challenges in maintaining yield and productivity in larger bioreactor setups.

Article Abstract

The effect of gradients of elevated glucose and low dissolved oxygen in the addition zone of fed-batch thermoinduced recombinant high cell density cultures can be evaluated through two-compartment scale-down models. Here, glucose was fed in the inlet of a plug flow bioreactor (PFB) connected to a stirred tank bioreactor (STB). cells diminished growth from 48.2 ± 2.2 g/L in the stage of RP production if compared to control (STB) with STB-PFB experiments, when residence time inside the PFB was 25 s (34.1 ± 3.5 g/L) and 40 s (25.6 ± 5.1 g/L), respectively. The recombinant granulocyte-macrophage colony-stimulating factor (rHuGM-CSF) production decreased from 34 ± 7% of RP in inclusion bodies (IB) in control cultures to 21 ± 8%, and 7 ± 4% during the thermoinduction production phase when increasing residence time inside the PFB to 25 s and 40 s, respectively. This, along with the accumulation of acetic and formic acid (up to 4 g/L), indicates metabolic redirection of central carbon routes through metabolic flow and mixed acid fermentation. Special care must be taken when producing a recombinant protein in heat-induced , because the yield and productivity of the protein decreases as the size of the bioreactors increases, especially if they are carried at high cell density.

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http://dx.doi.org/10.1080/10826068.2024.2347403DOI Listing

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