Unstructured model for L-lysine fermentation under controlled dissolved oxygen

Biotechnol Prog. 2003 Jul-Aug;19(4):1387-90. doi: 10.1021/bp034019s.

Abstract

An unstructured model was developed for batch cultivation of Corynebacterium lactofermentum (ATCC 21799) under controlled dissolved oxygen. The model is capable of predicting batch experiments performed at various initial substrate concentrations. By extending the batch culture model to a fed-batch model and using a heuristic approach to optimize the fed-batch cultivation, it is shown that fed-batch cultivation is superior to batch operation due to increased productivity at high substrate concentrations.

Publication types

  • Comparative Study
  • Evaluation Study
  • Research Support, Non-U.S. Gov't
  • Validation Study

MeSH terms

  • Bioreactors / microbiology*
  • Computer Simulation
  • Corynebacterium / growth & development*
  • Corynebacterium / metabolism*
  • Glucose / metabolism*
  • Lysine / biosynthesis*
  • Models, Biological*
  • Oxygen / metabolism*
  • Oxygen Consumption / physiology*
  • Reproducibility of Results
  • Sensitivity and Specificity

Substances

  • Glucose
  • Lysine
  • Oxygen