Sustainable and economical
production of butanol via acetone-butanol-ethanol
(ABE) fermentation faces several major challenges, including high
feedstock cost, low butanol yield, and low butanol productivity. To
address these challenges, low-cost food waste was used as feedstock
for ABE production in batch and continuous immobilized-cell fermentation
by a recombinant high-butanol production strain Clostridium
saccharoperbutylacetonicum deltptabuk. Food waste
was first liquefied and saccharified to obtain fermentable sugars.
After that, food waste hydrolysates were fed into both batch and continuous
immobilized-cell fermentation systems to produce ABE. In the batch
fermentation, only 14.32 g/L ABE was produced using food waste hydrolysates
medium. However, when food waste hydrolysate medium was fed into the
continuous immobilized-cell fermentation, remarkable increases of
ABE production, yield, and productivity were achieved. At the dilution
rate of 0.1 h–1, 19.65 g/L ABE was produced with
an ABE yield of 0.43. At the dilution rate of 0.39 h–1, the highest ABE productivity (4.56 g/L/h) was obtained, which was
23 times higher than that in the batch fermentation. This study for
the first time demonstrated efficient conversion of food waste to
butanol via continuous immobilized-cell fermentation to achieve high
titer and productivity, which would potentially support the advanced
utilization of organic waste materials for biofuel production.