In an attempt to elucidate the impact of substrate accessibility to cellulases on the susceptibility of lignocellulosic substrates to enzymatic hydrolysis, a hydrogen peroxide treated, Douglas fir kraft pulp was dried using several methods with varying levels of intensity. Oven-drying at 50 and 100 degrees C, air-drying, and freeze-drying methods were employed to remove the interfibrillar water from the pulp samples. Subsequently, the never-dried and variably dried pulps were hydrolyzed using a commercial cellulase preparation supplemented with additional beta-glucosidase. Drying reduced the susceptibility of the substrates to enzymatic hydrolysis, which can be attributed to the hornifying effect that drying has on fibers. This effect was more pronounced for the fibers that were oven-dried at 100 degrees C (23% reduction) and 50 degrees C (15% reduction), and there was a good correlation between the Simons's stain results and the enzymatic digestibility of the dried pulps. These observations indicated that drying significantly reduced the population of larger pores and that the partial closure of larger pores created a large number of smaller pores that were not accessible to the displacement dye molecules (orange dye). The inaccessibility of the cellulose to the enzymes, due to the collapse or closure of the large pores, appears to be the primary reason for the lower susceptibility of the dried pulps to enzymatic hydrolysis.
One of the limiting factors restricting the effective and efficient bioconversion of softwood-derived lignocellulosic residues is the recalcitrance of the substrate following pretreatment. Consequently, the ensuing enzymatic process requires relatively high enzyme loadings to produce monomeric carbohydrates that are readily fermentable by ethanologenic microorganisms. In an attempt to circumvent the need for larger enzyme loadings, a simultaneous physical and enzymatic hydrolysis treatment was evaluated. A ball-mill reactor was used as the digestion vessel, and the extent and rate of hydrolysis were monitored. Concurrently, enzyme adsorption profiles and the rate of conversion during the course of hydrolysis were monitored. alpha-Cellulose, employed as a model substrate, and SO2-impregnated steam-exploded Douglas-fir wood chips were assessed as the cellulosic substrates. The softwood-derived substrate was further posttreated with water and hot alkaline hydrogen peroxide to remove >90% of the original lignin. Experiments at different reaction conditions were evaluated, including substrate concentration, enzyme loading, reaction volumes, and number of ball beads employed during mechanical milling. It was apparent that the best conditions for the enzymatic hydrolysis of alpha-cellulose were attained using a higher number of beads, while the presence of air-liquid interface did not seem to affect the rate of saccharification. Similarly, when employing the lignocellulosic substrate, up to 100% hydrolysis could be achieved with a minimum enzyme loading (10 filter paper units/g of cellulose), at lower substrate concentrations and with a greater number of reaction beads during milling. It was apparent that the combined strategy of simultaneous ball milling and enzymatic hydrolysis could improve the rate of saccharification and/or reduce the enzyme loading required to attain total hydrolysis of the carbohydrate moieties.
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