In the present work, factorial design and response surface techniques were
used in combination with modeling and simulation to design and optimize an
industrial bioprocess. Alcoholic fermentation process with multiple stages
was considered. The fermentation system is composed of four ideal continuou
s-stirred tank reactors (ICSTR), linked in series,with cell recycling. Oper
ational conditions for maximal yield and productivity were determined with
ten parameters under consideration: temperature (four stages), residence ti
me for each stage, cell recycling concentration, and the fraction of fresh
medium fed into the second fermentation stage. Initially, screening design
methodology was used to evaluate the process variables which were relevant
in relation to yield and productivity. Five statistically significant param
eters for each response were selected and utilized in factorial design in o
rder to optimize the process. With the models obtained from the factorial d
esign, response surfaces were generated, and the productivity improved to 1
2 g/l.h (an increase of 52% in relation to the control version of the biopr
ocess), while maintaining the high yield of 86.28% (99.1% conversion). (C)
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