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Related Concept Videos

Bioreactor Design and Operational System01:29

Bioreactor Design and Operational System

Bioreactors are engineered vessels designed to cultivate microorganisms under controlled conditions for industrial bioprocessing. They maintain sterility and allow precise regulation of pH, temperature, oxygen, and nutrient levels to optimize microbial growth and metabolite production. Bioreactors range from small laboratory units of 1 liter to industrial systems holding up to 500,000 liters, though only about 75% of their volume is actively used for fermentation. The remaining headspace...
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Maintaining optimal conditions within fermenters is essential for maximizing microbial productivity and ensuring process efficiency. This lesson focuses on key parameters—temperature, foam, pH, carbon dioxide, oxygen, and pressure—and their precise measurement and control strategies in fermentation systems.Temperature ControlTemperature regulation is critical due to the exothermic nature of many fermentation processes. In small laboratory fermenters, temperature is commonly monitored using...
Bioreactor Controls-II01:18

Bioreactor Controls-II

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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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...
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...
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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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A Novel Bioreactor for High Density Cultivation of Diverse Microbial Communities
08:13

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Published on: December 25, 2015

Liquid-phase mass transfer coefficients in bioreactors.

Y Kawase1, B Halard, M Moo-Young

  • 1Biochemical Engineering Group, Department of Chemical Engineering, University of Waterloo, Waterloo, Ontario, Canada.

Biotechnology and Bioengineering
|May 1, 1992
PubMed
Summary

A new model predicts liquid-phase mass transfer coefficients in bioreactors using surface renewal theory. The model shows good agreement with experimental data from bubble column reactors, aiding bioprocess optimization.

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Area of Science:

  • Biochemical Engineering
  • Mass Transfer Phenomena
  • Bioreactor Design

Background:

  • Accurate liquid-phase mass transfer coefficients are crucial for optimizing bioreactor performance.
  • Existing models may not fully capture the complexities of mass transfer in various bioreactor types.

Purpose of the Study:

  • To develop and validate a theoretical model for predicting liquid-phase mass transfer coefficients in bioreactors.
  • To assess the model's applicability to different fermentation broths and bioreactor configurations.

Main Methods:

  • Development of a theoretical model based on the surface renewal concept.
  • Experimental determination of volumetric mass transfer coefficients in a bench-scale bubble column reactor.
  • Estimation of specific surface area using established correlations.

Main Results:

  • The proposed surface renewal model provides reasonable predictions of liquid-phase mass transfer coefficients.
  • Model predictions show good agreement with experimental data for Chaetomium cellulolyticum fermentation broth and carboxymethyl cellulose media.
  • Validation against literature data from bubble column and stirred tank bioreactors supports the model's generalizability.

Conclusions:

  • The surface renewal concept offers a viable theoretical basis for modeling liquid-phase mass transfer in bioreactors.
  • The developed model can aid in the design and scale-up of bioreactors for bioprocesses.
  • Further studies can explore model refinement for more complex systems and operating conditions.