Skip to main content Accessibility help
×
Hostname: page-component-84b7d79bbc-lrf7s Total loading time: 0 Render date: 2024-07-25T06:36:45.169Z Has data issue: false hasContentIssue false

12 - Optimization for Cell Mass Production

Published online by Cambridge University Press:  05 April 2013

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

Summary

Optimization of bioprocesses is very important because these processes require capital-intensive plants, yield products that are low in concentration, and sometimes use expensive raw materials. The objective of bioprocess optimization is to maximize the profit of the process. More specifically, it frequently involves the maximization of the volumetric productivity, metabolite concentration, conversion, or yield and minimization of capital and operating costs or time to achieve a desired conversion.

Vital to the success of optimization methods is the development of mathematical models that describe adequately the behavior of the process under various conditions and therefore provide quantitative relationships between the outcome (outputs) and the manipulated variables (inputs) of the process. Some models contain a number of process parameters that need to be determined directly or indirectly from experimental data. The optimal control is aimed at achieving process optimization. A model being the foundation for process optimization and control, any increase in complexity of the model is justified only if it results in a significant improvement in the process performance. In light of the complex nature of the microbial and cellular processes, improved on-line measurement and data acquisition methods are of central importance to optimization of these bioprocesses. In this chapter, we deal with the optimization of bioreactors that are modeled by ordinary differential equations, which results from the material balances of species involved: the cells, substrates, products, intermediates, nutrients, various enzymes, and other chemical entities, as we have seen in previous chapters. In this chapter, we consider an impulse optimization through the application of PMP, which is most well suited for processes described by a set of ordinary differential equations.

Type
Chapter
Information
Fed-Batch Cultures
Principles and Applications of Semi-Batch Bioreactors
, pp. 227 - 297
Publisher: Cambridge University Press
Print publication year: 2013

Access options

Get access to the full version of this content by using one of the access options below. (Log in options will check for institutional or personal access. Content may require purchase if you do not have access.)

References

Pontryagin, L. S., Boltyanski, V. G., Gamkrelidge, R. V., and Mischenko, E. F. 1962. The Mathematical Theory of Optimal Processes. Wiley-Interscience.Google Scholar
Berber, R., Pertev, C., and Tucker, M. 1999. Optimization of feeding profiles for baker's yeast production by dynamic programming. Bioprocess Engineering 20: 263–269.CrossRefGoogle Scholar
Modak, J. M., and Lim, H. C. 1989. Simple nonsingular control approach to fed-batch fermentation optimization. Biotechnology Bioengineering 33: 11–15.CrossRefGoogle ScholarPubMed
Weigand, W. A. 1981. Maximum cell productivity by repeated fed-batch culture, constant yield case. Biotechnology Bioengineering 23: 249–266.CrossRefGoogle Scholar
San, K.-Y., and Stephanopoulos, G. 1989. Optimization of fed-batch penicillin fermentation: A case of singular optimal control with state constraints. Biotechnology Bioengineering 34: 72–78.CrossRefGoogle ScholarPubMed
Shin, S. H., and Lim, H. C. 2007. Cell-mass maximization in fed-batch culture: Sufficient conditions for singular arc and optimal feed rate profiles. Bioprocess and Biosystems Engineering 29: 335–347.CrossRefGoogle Scholar
Shin, S. H., and Lim, H. C. 2007. Optimization of metabolite production in fed-batch culture: Use of sufficiency and characteristics of singular arc and properties of adjoint vector in numerical computation. Industrial Engineering Chemistry Research 46: 2526–2534.CrossRefGoogle Scholar
Shin, H., and Lim, H. C. 2007. Maximization of metabolite in fed-batch cultures: Sufficient conditions for singular arc and optimal feed rate profiles. Biochemical Engineering Journal 37: 62–74.CrossRefGoogle Scholar
Lee, J. H., Lim, H. C., and Hong, J. 1997. Application of non-singular transformation to on-line optimal control of poly-β-hydroxybutyrate fermentation. Journal of Biotechnology 55: 135–150.CrossRefGoogle Scholar
Miele, A. 1962. Optimization Technique, ed. Leitman, G.Academic Press.Google Scholar
Ohno, H., Nakanishi, E., and Takamatsu, T. 1976. Optimal control of a semi-batch fermentation. Biotechnology Bioengineering 18: 847–864.CrossRefGoogle Scholar
Lee, J. H., Lim, H. C., Yoo, Y. H., and Park, Y. H. 1999. Optimization of feed rate profile for the monoclonal antibody production. Bioprocess Engineering 20: 137–146.CrossRefGoogle Scholar
Lee, J. H., Lim, H. C., and Kim, S. I. 2001. A nonsingular optimization approach to the feed rare profile optimization of fed-batch cultures. Bioprocess and Biosystems Engineering 24: 115–125.Google Scholar
Jayant, A., and Pushpavanam, S. 1998. Optimization of a biochemical fed-batch reactor transition from a non-singular to a singular problem. Industrial Engineering Chemistry Research 37: 4314–4321.CrossRefGoogle Scholar
Pushpavanam, S., Rao, S., and Kahn, I. 1999. Optimization of a biochemical fed- batch reactor using sequential quadratic programming. Industrial Engineering Chemistry Research 38: 1998–2004.CrossRefGoogle Scholar
Kelley, H. J. 1965. A transformation approach to singular subarcs in optimal trajectory and control problems. Journal of the Society for Industrial Applied Mathematics, Control 2: 234–241.CrossRefGoogle Scholar
Contois, D. 1959. Relationship between population density and specific growth rate of continuous cultures. Journal of General Microbiology 21: 40–50.CrossRefGoogle ScholarPubMed
Weigand, W. A., Lim, H. C., Creagan, C., and Mohler, , , R. 1979. Optimization of a repeated fed-batch reactor for maximum cell productivity. Biotechnology and Bioengineering Symposium 9: 335–348.Google Scholar
Modak, J. M., and Lim, H. C. 1989. Optimal operation of fed-batch bioreactors with two control variables. Chemical Engineering Journal 42: B15–B24.CrossRefGoogle Scholar

Save book to Kindle

To save this book to your Kindle, first ensure coreplatform@cambridge.org is added to your Approved Personal Document E-mail List under your Personal Document Settings on the Manage Your Content and Devices page of your Amazon account. Then enter the ‘name’ part of your Kindle email address below. Find out more about saving to your Kindle.

Note you can select to save to either the @free.kindle.com or @kindle.com variations. ‘@free.kindle.com’ emails are free but can only be saved to your device when it is connected to wi-fi. ‘@kindle.com’ emails can be delivered even when you are not connected to wi-fi, but note that service fees apply.

Find out more about the Kindle Personal Document Service.

Available formats
×

Save book to Dropbox

To save content items to your account, please confirm that you agree to abide by our usage policies. If this is the first time you use this feature, you will be asked to authorise Cambridge Core to connect with your account. Find out more about saving content to Dropbox.

Available formats
×

Save book to Google Drive

To save content items to your account, please confirm that you agree to abide by our usage policies. If this is the first time you use this feature, you will be asked to authorise Cambridge Core to connect with your account. Find out more about saving content to Google Drive.

Available formats
×