Acetone-butanol-ethanol (ABE) fermentation process can be exploited for the generation of butanol as biofuel

however it does need to overcome its low volumetric solvent productivity before it can commercially compete with fossil fuel technologies. In this regard

mathematical modelling and simulation analysis are tools that can serve as the base for process engineering development of biological systems. In this work

a novel phenomenological kinetic model of Clostridium acetobutylicum ATCC 824 was considered as a benchmark system to evaluate the behaviour of an ABE fermentation under different process configurations using both free and immobilized cells:single stage batch operation

fed-batch

single stage Continuous Stirred Tank Reactor (CSTR) and multistage CSTRs with and without biomass recirculation. The proposed model achieved a linear correlation index r

2

=0.9952 and r

2

=0.9710 over experimental data for free and immobilized cells respectively. The predicted maximum butanol concentration and productivity obtained were 13.08 g·L

-1

and 1.9620 g·L

-1

·h

-1

respectively

which represents

an increase of 1.01% and 990% versus the currently developed industrial scale process reported currently into the literature. These results provide a reliable platform for the design and optimization of the ABE fermentation system and showcase the adequate predictive nature of the proposed model.