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Scale-Up Processes01:14

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The scale-up of microbial fermentation processes is essential in industrial biotechnology, allowing the transition from laboratory-scale experiments to commercial-scale production while aiming to maintain product yield and quality. This process requires meticulous adjustment of equipment design, process parameters, and contamination control strategies to accommodate increasing culture volumes.At the laboratory scale, cultures are typically maintained in 1 to 10-liter glass or autoclavable...
Bioreactor Design and Operational System01:29

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Growth media provide essential nutrients that support cell growth and metabolism, thereby enhancing the yield of valuable products such as enzymes, antibiotics, and biomass. Designing an effective growth medium involves balancing all components to prevent nutrient limitations or toxic excesses, both of which can impair growth and reduce product yields.Composition of a Typical Growth MediumA typical growth medium contains carbon and nitrogen sources, salts, vitamins, trace elements, and...
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Upstream processing represents a critical phase in biomanufacturing, wherein biological systems such as microorganisms, mammalian cells, or insect cells are cultivated to produce therapeutic proteins, vaccines, enzymes, or other biologically derived products. This phase encompasses all steps from the selection and genetic manipulation of the production organism to the cultivation of cells in bioreactors under tightly controlled environmental conditions.Host Selection and Genetic OptimizationThe...
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Strain improvement is a foundational strategy in industrial microbiology aimed at maximizing microbial productivity, particularly because natural isolates typically yield commercially valuable products in very low concentrations. Although optimizing the culture medium and environmental conditions can improve yields, these adjustments are inherently limited by the organism’s genetic potential. As a result, the focus shifts toward genetic modifications to enhance biosynthetic capacity. The...
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In aerobic fermentations, oxygen is vital for microbial growth and metabolite production. Since air comprises only about 20% oxygen and the gas is poorly soluble in water—just 9 ppm at 20°C—supplying sufficient oxygen becomes a critical challenge, especially in high-demand processes like yeast growth or citric acid production. Even a fully saturated broth may offer only a few seconds of oxygen availability.To address this, sterile or scrubbed air is introduced into the fermentor via a sparger...

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Comparative Analysis of Bioreactor Design and Scale-Up for Cultivated Meat Using Monte Carlo-Based Timescale

Pieter Jan Theodoor Brorens1, Marcel Ottens1, Cees Haringa1

  • 1Faculty of Applied Sciences, Department of Biotechnology, Delft University of Technology, Delft, Netherlands.

Biotechnology and Bioengineering
|July 14, 2026
PubMed
Summary

This study compares bioreactor designs for cultivated meat production, finding that stirred tank reactors and airlift reactors show promise for scale-up. The research provides a framework to accelerate bioreactor selection for sustainable meat alternatives.

Keywords:
Monte Carlo simulationbioreactor designcultivated meatscale‐uptimescale analysis

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Area of Science:

  • Biotechnology
  • Chemical Engineering
  • Food Science

Background:

  • Cultivated meat offers a sustainable alternative to conventional livestock.
  • Scaling up cultivated meat production faces significant bioreactor design challenges for mammalian cell suspension cultures.

Purpose of the Study:

  • To comparatively analyze stirred tank reactors (STRs), bubble columns (BCs), and airlift reactors (ALRs) for large-scale cultivated meat production.
  • To develop a predictive framework for evaluating bioreactor performance and identifying scale-up limitations.

Main Methods:

  • A Monte Carlo-based framework combined with timescale analysis was used to evaluate mixing and gas-liquid mass transfer.
  • Simulations assessed reactor performance up to 160 m³ against constraints like oxygen transfer, CO2 accumulation, and cell damage.
  • Hypothetical killing volume (HKV) modeled bubble-induced cell damage.

Main Results:

  • Mixing and oxygen transfer are primary limitations across all reactor types at large scales.
  • Bubble columns and airlift reactors face additional constraints related to gas-phase depletion and downcomer residence times.
  • Incorporating shear protectants like Pluronic F-68 and geometric optimization of STRs/ALRs significantly improved predicted performance, reaching up to 119 g L⁻¹.

Conclusions:

  • The developed framework enables rapid screening of bioreactor designs without complex mass balance calculations.
  • This approach provides insights into scale-up risks and guides experimental validation for cultivated meat process development.
  • Optimized STRs and ALRs show potential for efficient, large-scale cultivated meat production.