The pretreatment reactor design allowed for improved milling, continuous sampling of hydrolysate, and controlled delivery of acid to the feedstock. Tube fermentation was used on both pretreatment hydrolysates and prepared stock solutions of varying glucose and furfural concentrations.
Hydrolysate samples with furfural to glucose selectivities of 0.56 or greater were expected to produce little to no ethanol, demonstrating threshold-like inhibitory effect of furfural on the fermentation process. Further, although increasing pretreatment operating temperatures yielded higher amounts of glucose in the hydrolysate, significant ethanol production was expected to occur only at our lowest temperature (125˚C), indicating that a higher glucose content was not the sole indicator of higher ethanol production. Expected ethanol yields in our experiments were calculated based on extrapolations made using data from stock solution fermentation and literature.