A maximum production strategy of lysine based on a simplified model derived from a metabolic reaction network.
The aim of this study is to develop a strategy for maximum production of a target product with a simplified model derived from a metabolic reaction network through an example of lysine production. Based on the model, a search for the optimal specific growth rate profile was conducted among the available conditions of batch fermentation based on the derived model, when the total fermentation time was fixed. The optimal specific growth rate was obtained as a boundary control: initially, the specific growth rate was maintained at a maximum value and was subsequently switched to a critical value giving the maximum specific production rate. To make the specific growth rate follow this optimal profile as accurately as possible in batch mode, first, an appropriate initial concentration of leucine was employed in the experiment. Second, the feeding strategy of leucine was further studied. The specific growth rate profile with feeding was closer to the optimal one and the amount of lysine produced at the final stage of fermentation was increased about twofold, compared to that in the batch fermentation. Finally, the strategy was summarized as an algorithm for general use of this method.
Department of Biotechnology, Graduate School of Engineering, Osaka University, Suita, Japan.
H
H
Shimizu
N
N
Takiguchi
H
H
Tanaka
S
S
Shioya
D019149:Bioreactors; D001709:Biotechnology; D003352:Corynebacterium / Q000254:growth & development / Q000378:metabolism; D005285:Fermentation; D005947:Glucose / Q000378:metabolism; D007930:Leucine / Q000378:metabolism; D008239:Lysine / Q000096:biosynthesis*; D008954:Models, Biological
D007930:Leucine; D005947:Glucose; D008239:Lysine