Computational algorithms for optimal feed rates for a class of fed‐batch fermentation: Numerical results for penicillin and cell mass production
- 1 September 1986
- journal article
- research article
- Published by Wiley in Biotechnology & Bioengineering
- Vol. 28 (9), 1408-1420
- https://doi.org/10.1002/bit.260280915
Abstract
Based upon the general characteristics of the optimal feed rate profiles presented in an earlier article, efficient computational algorithms have been developed for fed‐batch fermentation processes described by four or less mass balance equations. These algorithms make computations of optimal substrate feed rate profiles straight forward and simple for various fed‐batch cultures for such products as antibiotics, amino acids, enzymes, alcohols, and cell mass. Numerical examples of penicillin fermentation and bacterial cell mass production are given in detail, illustrating the use of these algorithms.This publication has 10 references indexed in Scilit:
- General characteristics of optimal feed rate profiles for various fed‐batch fermentation processesBiotechnology & Bioengineering, 1986
- A note on the optimality criteria for maximum biomass production in a fed-batch fermentorBiotechnology & Bioengineering, 1984
- Optimal substrate profile for antibiotic fermentationsBiotechnology & Bioengineering, 1981
- Evaluation of feeding strategies in carbon-regulated secondary metabolite production through mathematical modelingBiotechnology & Bioengineering, 1981
- An experimental investigation of stability and multiplicity of steady states in a biological reactorAIChE Journal, 1981
- Maximum cell productivity by repeated fed-batch culture for constant yield caseBiotechnology & Bioengineering, 1981
- Optimal control of a semibatch fermentationBiotechnology & Bioengineering, 1976
- Effect of Growth Rate on the Synthesis of Penicillin by Penicillium chrysogenum in Batch and Chemostat CulturesApplied Microbiology, 1967
- PENICILLIN FROM CHEMICALLY DEFINED MEDIAIndustrial & Engineering Chemistry, 1953