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Updated: Jun 10, 2026

High-throughput Screening of Recalcitrance Variations in Lignocellulosic Biomass: Total Lignin, Lignin Monomers, and Enzymatic Sugar Release
Published on: September 15, 2015
Optimizing cellulase usage for improved mixing and rheological properties of acid-pretreated sugarcane bagasse
Claudia C Geddes1, James J Peterson, Michael T Mullinnix
1Department of Microbiology & Cell Science, University of Florida, Box 110700, Gainesville, FL 32611, USA.
Abstract:
Consolidation of bioprocessing steps with lignocellulose is limited by hydrolysate toxicity, the fibrous nature of suspensions, and low activity of cellulase enzymes. Combinations of enzyme dose and treatment conditions improved the flow properties and pumping of acid-pretreated sugarcane bagasse slurries (10% dry weight). Low levels of cellulase enzyme (0.1 and 0.5 FPU/g dry weight acid-pretreated bagasse) were found to reduce viscosities by 77-95% after 6 h, solubilizing 3.5% of the bagasse dry weight. Flow of slurries through small funnels was a useful predictor of success with centrifugal and diaphragm pumps. Equations were derived that describe viscosity and solubilized carbohydrates as a function of time and cellulase dosage. Blending of acid-pretreated bagasse (10% dry weight) with suspensions of acid-pretreated bagasse (10% dry weight) that had been previously digested with cellulase enzymes (low viscosity) did not increase viscosity in a linear fashion. Viscosity of these mixtures remained relatively constant until a threshold level of new fiber was reached, followed by a rapid increase with further additions. Up to 35% fresh acid-pretreated bagasse could be blended with enzyme-digested fiber (5.0 FPU/g dry weight acid-pretreated fiber; 6 h) with only a modest increase in viscosity. The smooth surfaces of enzyme-treated fiber are proposed to hinder the frequency and extent of interactions between fibrils of fresh fiber particles (acid-pretreated) until a threshold concentration is achieved, after which fiber interactions and viscosity increase dramatically. These results were used to model the viscosity in an ideal continuous stirred tank reactor (liquefaction) as a function of residence time and enzyme dosage.
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