Abstract
Fermentation optimization involves potentially conflicting multiple objectives such as product concentration and production media cost. Simultaneous optimization of these objectives would result in a multiobjective optimization problem, which is characterized by a set of multiple solutions, knows as pareto optimal solutions. These solutions gives flexibility in evaluating the trade-offs and selecting the most suitable operating policy. Here, ε-constraint approach was used to generate the pareto solutions for two objectives: product concentration and product per unit cost of media, for batch and fed batch operations using process model for Amycolatopsis balhimycina, a glycopeptide antibiotic producer. This resulted in a set of several pareto optimal solutions with the two objectives ranging from (0.75gl−1, 3.97g$-1) to (0.44gl−1, 5.19g$-1) for batch and from (1.5gl−1, 5.46g$-1) to (1.1gl−1, 6.34g$-1) for fed batch operations. One pareto solution each for batch and for fed batch mode was experimentally validated.
Original language | English |
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Journal | Bioresource Technology |
Volume | 102 |
Issue number | 13 |
Pages (from-to) | 6951-6958 |
ISSN | 0960-8524 |
DOIs | |
Publication status | Published - 2011 |
Keywords
- Batch
- Multi-objective optimization
- Glycopeptide antibiotic
- Fed batch
- Pareto optimal