The ABE (acetone, butanol, ethanol) fermentation is characterized by its low productivity. In this paper, this issue is overcome with an innovative industrial process that employs the flash fermentation technology. The process consists of three interconnected units, as follows: fermentor, cell retention system (tangential microfiltration) and vacuum flash vessel (responsible for the continuous recovery of butanol from the broth). The dynamic behaviour of the process is described by a non-linear mathematical model with kinetic parameters determined experimentally. From simulations of the mathematical model the dynamic characteristic of the process were investigated. Analyzes of the open-loop dynamic behavior of the process, after step perturbations in the manipulated variables, determined the best control structures for the process.
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Univ Naples Federico II, Dipartimento Ingn Chim Mat & Prod Ind, Naples, ItalyUniv Naples Federico II, Dipartimento Ingn Chim Mat & Prod Ind, Naples, Italy
Procentese, Alessandra
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Raganati, Francesca
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Olivieri, Giuseppe
Russo, Maria Elena
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CNR, Ist Ric Combust, Bologna, ItalyUniv Naples Federico II, Dipartimento Ingn Chim Mat & Prod Ind, Naples, Italy