Figure 3From: A highly efficient dilute alkali deacetylation and mechanical (disc) refining process for the conversion of renewable biomass to lower cost sugarsGlucose (a) and xylose (b) yield during enzymatic hydrolysis of DCS and DRDCS. The digestions were carried out at 1% (w/w) cellulose loadings with enzyme loadings of 32 mg/g cellulose CTec3 and 5 mg/g cellulose HTec3. Panel a: monomeric glucose yield; panel b: monomeric xylose yield.Back to article page