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Scale-Up Processes01:14

Scale-Up Processes

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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Fermentation is a foundational biotechnological process used to produce pharmaceuticals, biofuels, enzymes, and food additives. Among industrial strategies, batch and continuous fermentation are the two most widely applied. Although both rely on microbial conversion of substrates into desired products, they differ markedly in operation, productivity, and suitability for specific applications.Batch fermentation occurs in a closed system in which nutrient media and inoculum are added at the...
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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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Continuous fermentation is a key strategy in industrial ethanol production, particularly when efficiency, scalability, and high yields are essential. This approach allows for uninterrupted operation and optimized resource utilization. The primary feedstock, corn starch, undergoes enzymatic hydrolysis facilitated by α-amylase and glucoamylase. These enzymes break down the starch into fermentable sugars such as glucose, which are readily assimilated by fermentative microorganisms.Fermentation...
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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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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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Design and Use of Multiplexed Chemostat Arrays
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Stable competitive coexistence in a continuous fermentor with size-selective properties.

B H Davison1, K Y San, G Stephanopoulos

  • 1Dept. of Chemical Engineering, California Institute of Technology Pasadena, CA 91125.

Biotechnology Progress
|June 23, 2010
PubMed
Summary

A novel reactor design enabled stable coexistence of Escherichia coli (E. coli) and Saccharomyces cerevisiae (yeast) in continuous culture by exploiting size differences for selective cell retention and removal.

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Area of Science:

  • Biotechnology and Bioprocessing
  • Microbial Ecology
  • Chemical Engineering

Background:

  • Achieving stable coexistence of microbial species with different growth rates in continuous culture is challenging.
  • Traditional continuous culture systems often lead to the washout of slower-growing species.
  • Size-based separation offers a potential strategy for managing mixed microbial populations.

Purpose of the Study:

  • To develop and evaluate a size-selective reactor for enabling stable coexistence of Escherichia coli and Saccharomyces cerevisiae.
  • To investigate the mechanisms of size-based cell retention and removal in a mixed culture.
  • To analyze the stability conditions for microbial coexistence in the developed reactor system.

Main Methods:

  • Construction of a continuous culture reactor with an inclined side-arm for enhanced cell sedimentation and recycling.
  • Utilizing differential cell size between Saccharomyces cerevisiae (larger) and Escherichia coli (smaller) for separation.
  • Performing stability analysis based on net removal rates as a function of cell concentration.
  • Experimental measurement of the net removal rate function using a separate system.

Main Results:

  • The size-selective reactor successfully maintained a stable mixed culture of E. coli and S. cerevisiae.
  • Larger yeast cells were preferentially retained and recycled, while smaller, faster-growing bacteria were removed.
  • Stability was achieved when the net yeast removal rate function was concave up, observed with growth in the settler at low biomass.

Conclusions:

  • Size-selective reactors can effectively manage mixed microbial cultures with different characteristics.
  • Enhanced sedimentation in an inclined side-arm facilitates preferential retention of larger cells.
  • Microbial growth within the settler can contribute to the stability of coexistence steady states in continuous culture.