Cover Image
close this bookRenewable biological systems for alternative sustainable energy production. (FAO Agricultural Services Bulletin - 128) (1997)
close this folderChapter 3 - Production of fuel alcohol from cellulosic biomass
close this folder3.5 Alcohol production using an integrated pilot plant
View the document(introduction...)
View the document3.5.1 Outline
View the document3.5.2 Pre-treatment of cellulosic biomass
View the document3.5.3 Cellulase production
View the document3.5.4 Saccharification of biomass
View the document3.5.5 Enzyme recovery from biomass
View the document3.5.6 Concentration of sugar solutions
View the document3.5.7 Alcohol fermentation
View the document3.5.8 Alcohol recovery

3.5.4 Saccharification of biomass

High-concentration saccharification was conducted by the batch method. An example using bagasse as the biomass source is shown in Fig. 3-12. Low-concentration saccharification was performed by the continuous method, the volume of biomass being adjusted to between 3 and 6%. A saccharification rate of 90 to 95%, was obtained after 5 to 7 hours of reaction, with only a small amount of unreacted biomass residue remaining after the reaction. Beech chips treated by steam explosion (Temp: 220°C2 pressure retention time: 5 min) were also subjected to the saccharification reaction for 24 hours, resulting in a saccharification rate of approximately 75 %. Table 3-7 summarizes cellulase requirements, for the saccharification of biomass, using cellulases prepared in our laboratory.


Figure 3.22 - Time course of high titer cellulase production by T. reesei CDU-11