Two-stage dilute acid pretreatment followed by enzymatic cellulose hydrolys
is is an effective method for obtaining high sugar yields from wood residue
s such as softwood forest thinnings. In the first-stage hydrolysis step, mo
st of the hemicellulose is solubilized using relatively mild conditions. Th
e soluble hemicellulosic sugars are recovered from the hydrolysate slurry b
y washing with water. The washed solids are then subjected to more severe h
ydrolysis conditions to hydrolyze approx 50% of the cellulose to glucose. T
he remaining cellulose can further be hydrolyzed with cellulase enzyme. Our
process simulation indicates that the amount of water used in the hemicell
ulose recovery step has a significant impact on the cost of ethanol product
ion. It is important to keep water usage as low as possible while maintaini
ng relatively high recovery of soluble sugars. To achieve this objective, a
prototype pilot-scale continuous countercurrent screw extractor was evalua
ted for the recovery of hemicellulose from pretreated forest thinnings. Usi
ng the 274-cm (9-ft) long extractor, solubles recoveries of 98, 91, and 77%
were obtained with liquid-to-insoluble solids (L/IS) ratios of 5.6, 3.4, a
nd 2.1, respectively. An empirical equation was developed to predict the pe
rformance of the screw extractor. This equation predicts that soluble sugar
recovery above 95% can be obtained with an L/IS ratio as low as 3.0.