The effect of particle size on hydrolysis reaction rates and rheological properties in cellulosic slurries

The effect of varying initial particle sizes on enzymatic hydrolysis rates and rheological properties of sawdust slurries is investigated. Slurries with four particle size ranges (33 µm<x≤75 µm, 150 µm<x≤180 µm, 295 µm<x≤425 µm, and 590 µm<x≤850 µm) were subjected to enzymatic hydrolysis using an enzyme dosage of 15 filter paper units per gram of cellulose at 50°C and 250 rpm in shaker flasks. At lower initial particle sizes, higher enzymatic reaction rates and conversions of cellulose to glucose were observed. After 72 h 50 and 55% more glucose was produced from the smallest size particles than the largest size ones, for initial solids concentration of 10 and 13% (w/w), respectively. The effect of initial particle size on viscosity over a range of shear was also investigated. For equivalent initial solids concentration, smaller particle sizes result in lower viscosities such that at a concentration of 10% (w/w), the viscosity decreased from 3000 cP for 150 µm<x≤180 µm particle size slurries to 61.4 cP for 33 µm<x≤75 µm particle size slurries. Results indicate particle size reduction may provide a means for reducing the long residence time required for the enzymatic hydrolysis step in the conversion of biomass to ethanol. Furthermore, the corresponding reduction in viscosity may allow for higher solids loading and reduced reactor sizes during large-scale processing.

[1]  M. Coughlan Enzymic hydrolysis of cellulose: An overview , 1992 .

[2]  A. Converse,et al.  Kinetics of enzymatic hydrolysis of lignocellulosic materials based on surface area of cellulose accessible to enzyme and enzyme adsorption on lignin and cellulose , 1990 .

[3]  Guido Zacchi,et al.  Adsorption of Trichoderma reesei CBH I and EG II and their catalytic domains on steam pretreated softwood and isolated lignin. , 2004, Journal of biotechnology.

[4]  An approach in mathematical modeling of an upflow packed‐bed reactor for enzymatic hydrolysis of wheat straw , 1989, Biotechnology and bioengineering.

[5]  K. Movagharnejad Modified shrinking particle model for the rate of enzymatic hydrolysis of impure cellulosic waste materials with enzyme reuse by the substrate replacement , 2005 .

[6]  L. Walker,et al.  The impact of initial particle size on the fragmentation of cellulose by the cellulase of thermomonospora fusca , 1991 .

[7]  A. Gusakov,et al.  Kinetics of the enzymatic hydrolysis of cellulose: 1. A mathematical model for a batch reactor process , 1985 .

[8]  James Y. Oldshue,et al.  Fluid Mixing Technology , 1983 .

[9]  Robert H. Falk,et al.  Recovering wood for reuse and recycling : a United States perspective , 2004 .

[10]  M. Holtzapple,et al.  Effect of structural features on enzyme digestibility of corn stover. , 2006, Bioresource technology.

[11]  Alvin L Young,et al.  The World Congress on Industrial Biotechnology and Bioprocessing , 2004, Environmental science and pollution research international.

[12]  I. Cullis,et al.  Effect of initial moisture content and chip size on the bioconversion efficiency of softwood lignocellulosics , 2004, Biotechnology and bioengineering.

[13]  Ignacio Ballesteros,et al.  Enhanced enzymatic hydrolysis of olive tree wood by steam explosion and alkaline peroxide delignification , 2006 .

[14]  Effect of transient heat transfer and particle size on acid hydrolysis of hardwood cellulose. , 1991 .

[15]  J N Saddler,et al.  Steam pretreatment of lignocellulosic material for enhanced enzymatic hydrolysis , 1987, Biotechnology and bioengineering.

[16]  Farzaneh Teymouri,et al.  Understanding factors that limit enzymatic hydrolysis of biomass , 2005, Applied biochemistry and biotechnology.

[17]  H. Grethlein,et al.  Common aspects of acid prehydrolysis and steam explosion for pretreating wood , 1991 .

[18]  L. Walker,et al.  Enzymatic hydrolysis of cellulose: An overview , 1991 .

[19]  Stephen E. Wald,et al.  Kinetics of the enzymatic hydrolysis of cellulose , 1984, Biotechnology and bioengineering.

[20]  Johan Karlsson,et al.  A model explaining declining rate in hydrolysis of lignocellulose substrates with cellobiohydrolase I (Cel7A) and endoglucanase I (Cel7B) of Trichoderma reesei , 2002, Applied biochemistry and biotechnology.

[21]  K. Kadam,et al.  Development and Validation of a Kinetic Model for Enzymatic Saccharification of Lignocellulosic Biomass , 2004, Biotechnology progress.

[22]  J N Saddler,et al.  Factors affecting cellulose hydrolysis and the potential of enzyme recycle to enhance the efficiency of an integrated wood to ethanol process , 2000, Biotechnology and bioengineering.