Ethanol production from concentrated oak wood hydrolysate was carried out t
o obtain a high ethanol concentration and a high ethanol yield. The effect
of added inhibitory compounds, which are typically produced in the pretreat
ment step of steam-explosion on ethanol fermentation, was also examined. p-
Hydroxybenzoic aldehyde, a lignin-degradation product, was the most inhibit
ory compound tested in this study. Compounds with additional methyl groups
had reduced toxicity and the aromatic acids were less toxic than the corres
ponding aldehydes. The lignin-degradation products were more inhibitory tha
n the sugar-derived products, such as furfural and 5-hydroxymethylfurfural
(HMF). Adaptation of yeast cells to the wood hydrolysate and detoxification
methods, such as using charcoal and overlime, had some beneficial effects
on ethanol production using the concentrated wood hydrolysate. After treatm
ent with charcoal and low-temperature sterilization, the yeast cells could
utilize the concentrated wood hydrolysate with 170 as well as 140 g/L gluco
se, and produce 69.9 and 74.2 g/L ethanol, respectively, with a yield of 0.
46-0.48 g ethanol/g glucose. In contrast, the cells could not completely ut
ilize untreated wood hydrolysate with 100 g/L glucose. Low-temperature ster
ilization, with or without charcoal treatment, was very effective for ethan
ol production when highly concentrated wood hydrolysates were used. Low-tem
perature sterilization has advantages over traditional detoxification metho
ds, such as using overlime, ion exchange, and charcoal, because of the redu
ction in the total cost of ethanol production.