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2 - Idealized Reactors and Fed-Batch Reactors

Published online by Cambridge University Press:  05 April 2013

Henry C. Lim
Affiliation:
University of California, Irvine
Hwa Sung Shin
Affiliation:
Inha University, Seoul
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Summary

Prior to presenting the principles of fed-batch operations, it is instructive to review quickly various forms of idealized reactors: batch, continuous, and semi-batch reactors. This will help in understanding the simplest form of fed-batch operation as equivalent to a continuous-stirred tank reactor (CSTR) followed by a batch reactor (BR). It becomes simple and easy to understand the operation of a fed-batch bioreactor as mimicking a dynamic CSTR followed by a BR to maximize the reaction rate or product yield. In other words, for a single reaction, the sufficient condition for superior performance of fed-batch operation is that the reaction rate and/or product yield show a maximum or decrease with the substrate concentration.

Basically, a fed-batch operation is preferred when the main or a side reaction rate exhibits a maximum or if the side reaction is more sensitive than the main reaction to reactant concentrations. Fed-batch operations can take advantage of the maximum rate or the sensitivity of side reactions (yield) by manipulating the substrate (reactant) concentration in the reactor.

Type
Chapter
Information
Fed-Batch Cultures
Principles and Applications of Semi-Batch Bioreactors
, pp. 19 - 32
Publisher: Cambridge University Press
Print publication year: 2013

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References

Hill, Charles G.. 1977. Introduction to Chemical Engineering Kinetics and Reactor Design. John Wiley.Google Scholar
Harriott, P. 2002. Chemical Reactor Design. Marcel Dekker.CrossRefGoogle Scholar
Levenspiel, O. 1999. Chemical Reaction Engineering. 3rd ed. John Wiley.Google Scholar
Fogler, H. Scott. 2006. Elements of Chemical Reaction Engineering. 4th ed. Prentice Hall.Google Scholar

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