Abstract
Batch kinetics for cultivation of Ralstonia eutropha, NRRL B 14690 featured 19.7 g/l
biomass and 10.89 g/l PHB accumulation in 60 h under statistically
optimized culture conditions. For in-depth understanding of culture
dynamics and for suitable reactor design a mathematical model was
developed. The model was highly instrumental in guiding the appropriate
experiments to optimize the process with minimum efforts. Offline
computer simulated fed-batch cultivations allowed selection of two
different nutrient (nitrogen (as urea) and fructose) feeding strategies.
Fed-batch fermentation, conducted by feeding nitrogen (as urea) (8
g/l) at the rate of 70 ml/h and fructose (300 g/l) at the rate of 80
ml/h simultaneously yielded 17.57 g/l PHB in 50 h with an overall
productivity of 0.35 g/l h. In another strategy, alternate feeding of the
nitrogen (as urea) (15 g/l) and fructose (350 g/l) at a flow rate of 80
ml/h resulted in PUB accumulation of 18.46 g/l in 40 h resulting in
overall productivity of 0.46 g/l h. Model-based fed-batch operation was
very helpful for over producing PHB by R. eutropha. The increase
in PHB productivity in fed-batch cultivation was almost 2.6 times
as compared to batch. (c) 2005 Elsevier B.V. All rights reserved.
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