Cellulase–lignin interactions—The role of carbohydrate-binding module and pH in non-productive binding

Non-productive cellulase adsorption onto lignin is a major inhibitory mechanism preventing enzymatic hydrolysis of lignocellulosic feedstocks. Therefore, understanding of enzyme–lignin interactions is essential for the development of enzyme mixtures and processes for lignocellulose hydrolysis. We have studied cellulase–lignin interactions using model enzymes, Melanocarpus albomyces Cel45A endoglucanase (MaCel45A) and its fusions with native and mutated carbohydrate-binding modules (CBMs) from Trichoderma reesei Cel7A. Binding of MaCel45A to lignin was dependent on pH in the presence and absence of the CBM; at high pH, less enzyme bound to isolated lignins. Potentiometric titration of the lignin preparations showed that negatively charged groups were present in the lignin samples and that negative charge in the samples was increased with increasing pH. The results suggest that electrostatic interactions contributed to non-productive enzyme adsorption: Reduced enzyme binding at high pH was presumably due to repulsive electrostatic interactions between the enzymes and lignin. The CBM increased binding of MaCel45A to the isolated lignins only at high pH. Hydrophobic interactions are probably involved in CBM binding to lignin, because the same aromatic amino acids that are essential in CBM–cellulose interaction were also shown to contribute to lignin-binding.     

The Influence of Hemicellulose and Lignin Removal on the Enzymatic Digestibility from Sugarcane Bagasse

Sugarcane bagasse (SCB) was pretreated with liquid hot water (LHW) and aqueous ammonia (AA), with the objective of investigating the influence of hemicellulose and lignin removal on the enzymatic digestibility and sugar recovery. The experimental results show that LHW and aqueous ammonia have a good performance in terms of hemicellulose dissolution and lignin removal respectively. The biggest xylan recovery of 74.3 % was obtained for LHW pretreatment at 160 °C, 5 %?w/v for 20 min with the xylan dissolution of 83.1 %. And the biggest lignin removal of 84.0 % was obtained for aqueous ammonia pretreatment at 160 °C, 10 %?w/v for 60 min. Moreover, the aperture and surface area of the sample were enlarged by the liquid hot water, which improves the accessibility of the substrate to the enzyme. The lignin removal caused by aqueous ammonia pretreatment can reduce the absorption of enzyme. In addition, the correlation between the compositional change and the enzymatic digestibility indicates that the removal of hemicellulose was more effective than lignin for destruction of the hemicellulose–lignin–cellulose structure.     

Analysis of lignin–carbohydrate and lignin–lignin linkages after hydrolase treatment of xylan–lignin,glucomannan–lignin and glucan–lignin complexes from spruce wood

Xylan–lignin (XL), glucomannan–lignin (GML) and glucan–lignin (GL) complexes were isolated from spruce wood, hydrolyzed with xylanase or endoglucanase/β-glucosidase, and analyzed by analytical pyrolysis and 2D-NMR. The enzymatic hydrolysis removed most of the polysaccharide moieties in the complexes, and the lignin content and relative abundance of lignin–carbohydrate linkages increased. Analytical pyrolysis confirmed the action of the enzymatic hydrolysis, with strong decreases of levoglucosane and other carbohydrate-derived products. Unexpectedly it also revealed that the hydrolase treatment alters the pattern of lignin breakdown products, resulting in higher amounts of coniferyl alcohol. From the anomeric carbohydrate signals in the 2D-NMR spectra, phenyl glycoside linkages (undetectable in the original complexes) could be identified in the hydrolyzed GML complex. Lower amounts of glucuronosyl and benzyl ether linkages were also observed after the hydrolysis. From the 2D-NMR spectra of the hydrolyzed complexes, it was concluded that the lignin in GML is less condensed than in XL due to its higher content in β-O-4′ ether substructures (62 % of side chains in GML vs 53 % in XL) accompanied by more coniferyl alcohol end units (16 vs 13 %). In contrast, the XL lignin has more pinoresinols (11 vs 6 %) and dibenzodioxocins (9 vs 2 %) than the GML (and both have ~13 % phenylcoumarans and 1 % spirodienones). Direct 2D-NMR analysis of the hydrolyzed GL complex was not possible due to its low solubility. However, after sample acetylation, an even less condensed lignin than in the GML complex was found (with up to 72 % β-O-4′ substructures and only 1 % pinoresinols). The study provides evidence for the existence of structurally different lignins associated to hemicelluloses (xylan and glucomannan) and cellulose in spruce wood and, at the same time, offers information on some of the chemical linkages between the above polymers.     

Kinetic modeling for enzymatic hydrolysis of pretreated creeping wild ryegrass

A semimechanistic multi‐reaction kinetic model was developed to describe the enzymatic hydrolysis of a lignocellulosic biomass, creeping wild ryegrass (CWR; Leymus triticoides). This model incorporated one homogeneous reaction of cellobiose‐to‐glucose and two heterogeneous reactions of cellulose‐to‐cellobiose and cellulose‐to‐glucose. Adsorption of cellulase onto pretreated CWR during enzymatic hydrolysis was modeled via a Langmuir adsorption isotherm. This is the first kinetic model which incorporated the negative role of lignin (nonproductive adsorption) using a Langmuir‐type isotherm adsorption of cellulase onto lignin. The model also reflected the competitive inhibitions of cellulase by glucose and cellobiose. The Matlab optimization function of “lsqnonlin” was used to fit the model and estimate kinetic parameters based on experimental data generated under typical conditions (8% solid loading and 15 FPU/g‐cellulose enzyme concentration without the addition of background sugars). The model showed high fidelity for predicting cellulose hydrolysis behavior over a broad range of solid loading (4–12%, w/w, dry basis), enzyme concentration (15–150 FPU/ g‐cellulose), sugar inhibition (glucose of 30 and 60 mg/mL and cellobiose of 10 mg/mL). In addition, sensitivity analysis showed that the incorporation of the nonproductive adsorption of cellulase onto lignin significantly improved the predictability of the kinetic model. Our model can serve as a robust tool for developing kinetic models for system optimization of enzymatic hydrolysis, hydrolysis reactor design, and/or other hydrolysis systems with different type of enzymes and substrates. Biotechnol. Bioeng. 2009;102: 1558–1569. © 2008 Wiley Periodicals, Inc.     

Adsorption of Trichoderma reesei CBH I and EG II and their catalytic domains on steam pretreated softwood and isolated lignin

The presence of lignin has shown to play an important role in the enzymatic degradation of softwood. The adsorption of enzymes, and their constituent functional domains on the lignocellulosic material is of key importance to fundamental knowledge of enzymatic hydrolysis. In this study, we compared the adsorption of two purified cellulases from Trichoderma reesei, CBH I (Cel7A) and EG II (Cel5A) and their catalytic domains on steam pretreated softwood (SPS) and lignin using tritium labeled enzymes. Both CBH I and its catalytic domain exhibited a higher affinity to SPS than EG II or its catalytic domain. Removal of cellulose binding domain decreased markedly the binding efficiency. Significant amounts of CBH I and EG II also bound to isolated lignin. Surprisingly, the catalytic domains of the two enzymes of T. reesei differed essentially in the adsorption to isolated lignin. The catalytic domain of EG II was able to adsorb to alkaline isolated lignin with a high affinity, whereas the catalytic domain of CBH I did not adsorb to any of the lignins tested. The results indicate that the cellulose binding domain has a significant role in the unspecific binding of cellulases to lignin.     

Novel Penicillium cellulases for total hydrolysis of lignocellulosics

The (hemi)cellulolytic systems of two novel lignocellulolytic Penicillium strains (Penicillium pulvillorum TUB F-2220 and P. cf. simplicissimum TUB F-2378) have been studied. The cultures of the Penicillium strains were characterized by high cellulase and β-glucosidase as well moderate xylanase activities compared to the Trichoderma reesei reference strains QM 6a and RUTC30 (volumetric or per secreted protein, respectively). Comparison of the novel Penicillium and T. reesei secreted enzyme mixtures in the hydrolysis of (ligno)cellulose substrates showed that the F-2220 enzyme mixture gave higher yields in the hydrolysis of crystalline cellulose (Avicel) and similar yields in hydrolysis of pre-treated spruce and wheat straw than enzyme mixture secreted by the T. reesei reference strain. The sensitivity of the Penicillium cellulase complexes to softwood (spruce) and grass (wheat straw) lignins was lignin and temperature dependent: inhibition of cellulose hydrolysis in the presence of wheat straw lignin was minor at 35 °C while at 45 °C by spruce lignin a clear inhibition was observed. The two main proteins in the F-2220 (hemi)cellulase complex were partially purified and identified by peptide sequence similarity as glycosyl hydrolases (cellobiohydrolases) of families 7 and 6. Adsorption of the GH7 enzyme PpCBH1 on cellulose and lignins was studied showing that the lignin adsorption of the enzyme is temperature and pH dependent. The ppcbh1 coding sequence was obtained using PCR cloning and the translated amino acid sequence of PpCBH1 showed up to 82% amino acid sequence identity to known Penicillium cellobiohydrolases.     

The isolation, characterization and effect of lignin isolated from steam pretreated Douglas-fir on the enzymatic hydrolysis of cellulose

Douglas-fir was SO₂-steam pretreated at different severities (190, 200, and 210 °C) to assess the possible negative effect of the residual and isolated lignins on the enzymatic hydrolysis of the steam pretreated substrates. When various isolated lignins were added to the Avicel hydrolysis reactions, the decrease in glucose yields ranged from 15.2% to 29.0% after 72 h. It was apparent that the better hydrolysis yields obtained at higher pretreatment severities were more a result of the greater accessibly of the cellulose rather than any specific change in the non-productive binding of the lignin to the enzymes. FTIR and ¹³C NMR characterization indicated that the lignin in the steam pretreated substrates became more condensed with increasing severity, suggesting that the cellulases were adsorbed to the lignin by hydrophobic interactions. Electrostatic interactions were also involved as the positively charged cellulase components were preferentially adsorbed to the lignins.     

Ether linkage between phenolic acids and lignin fractions from wheat straw

The bonding of the bound-phenolic acids present in three lignin preparations isolated from wheat straw where determined. p-Coumaric acid was mainly ester-linked whereas 35–75% of the recovered ferulic acid was ether-linked to milled straw lignin or enzyme lignin. Ferulic acid ethers accounted for 1.1% dry wt of alkali extracted lignin and might explain the high solubility of Gramineae lignins in soda. Isolated lignins were associated to hemicelluloses, principally arabinoglucuronoxylans. The possible existence of ferulic acid cross-links between lignin and arabinoglucuronoxylans is discussed.     

Comparison of different pretreatment methods for lignocellulosic materials. Part I: conversion of rye straw to valuable products

The conversion of lignocellulose to valuable products requires I: a fractionation of the major components hemicellulose, cellulose, and lignin, II: an efficient method to process these components to higher valued products. The present work compares liquid hot water (LHW) pretreatment to the soda pulping process and to the ethanol organosolv pretreatment using rye straw as a single lignocellulosic material. The organosolv pretreated rye straw was shown to require the lowest enzyme loading in order to achieve a complete saccharification of cellulose to glucose. At biomass loadings of up to 15% (w/w) cellulose conversion of LHW and organosolv pretreated lignocellulose was found to be almost equal. The soda pulping process shows lower carbohydrate and lignin recoveries compared to the other two processes. In combination with a detailed analysis of the different lignins obtained from the three pretreatment methods, this work gives an overview of the potential products from different pretreatment processes.     

Elicitor-Induced Spruce Stress Lignin (Structural Similarity to Early Developmental Lignins)

Suspension cultures of Picea abies (L.) Karst released polymeric material into the culture medium when treated with an elicitor preparation from the spruce needle pathogen Rhizosphaera kalkhoffii. The presence of lignin (about 35%, w/w) was demonstrated by phloroglucinol/HCI reactivity and quantitation with thioglycolic acid. Carbohydrate (about 14%, w/w) and protein (about 32%, w/w) were also detected. Amino acid analysis revealed that hydroxyproline and proline predominated. Thioacidolysis and subsequent Raney nickel desulfurization allowed the analysis of lignin-building units and interunit bonds. Compared with spruce wood lignin, an approximately 20-fold higher relative amount of p-hydroxyphenyl units was determined. A high content of p-hydroxyphenyl units is typical for certain developmental lignins, such as conifer compression wood and middle lamella lignins, as well as all induced cell culture lignins so far analyzed. Cross-linkages of the pinoresinol type ([beta]-[beta]) in the excreted cell culture lignin were markedly increased, whereas [beta]-1 interunit linkages were decreased relative to spruce wood lignin. The amount and nature of cross-linkages were shown to be intermediate between those in wood lignin and in enzymatically prepared lignins. In summary, the elicitor-induced stress lignin was excreted as a lignin-extensin complex that closely resembled early developmental lignins.     

An integrative process of bioconversion of oil palm empty fruit bunch fiber to ethanol with on-site cellulase production

The aim of this study was to efficiently convert oil palm empty fruit bunch fiber (OPEFB), one of the most commonly generated lingo-wastes in Southeast Asia, into both cellulase and bioethanol. The unprocessed cellulase crude (37.29 %) produced under solid-state fermentation using OPEFB as substrate showed a better reducing sugar yield using filter paper than the commercial enzyme blend (34.61 %). Organosolv pretreatment method could efficiently reduce hemicellulose (24.3–18.6 %) and lignin (35.2–22.1 %) content and increase cellulose content (40.5–59.3 %) from OPEFB. Enzymatic hydrolysis of pretreated OPEFB using the crude cellulase with 20 % solid content, enzyme loading of 15 FPU/g OPEFB at 50 °C, and pH 5.5 resulted in a OPEFB hydrolysate containing 36.01 g/L glucose after 72 h. Fermentation of the hydrolysate medium produced 17.64 g/L ethanol with 0.49 g/g yield from glucose and 0.088 g/g yield from OPEFB at 8 h using Saccharomyces cerevisiae.     

Characterization of a NaCl-tolerant β-N-acetylglucosaminidase from <Emphasis Type="Italic">Sphingobacterium</Emphasis> sp. HWLB1

β-N-Acetylglucosaminidases serve important biological functions and various industrial applications. A glycoside hydrolase family 3 β-N-acetylglucosaminidase gene was cloned from Sphingobacterium sp. HWLB1 and expressed in Escherichia coli BL21 (DE3). The purified recombinant enzyme (rNag3HWLB1) showed apparent optimal activity at pH 7.0 and 40 °C. In the presence of 0.5–20.0 % (w/v) NaCl, the activity and stability of rNag3HWLB1 were slightly affected or not affected. The enzyme could even retain 73.6 % activity when 30.0 % (w/v) NaCl was added to the reaction mixture. The half-life of the enzyme was approximately 10 min at 37 °C without the addition of NaCl. However, the enzyme was stable at 37 °C in the presence of 3.0 % (w/v) NaCl. A large negatively charged surface in the catalytic pocket of the enzyme was observed and might contribute to NaCl tolerance and thermostability improvement. The degree of synergy between a commercial endochitinase and rNag3HWLB1 on chitin enzymatic degradation ranged from 3.11 to 3.74. This study is the first to report the molecular and biochemical properties of a NaCl-tolerant β-N-acetylglucosaminidase.     

Utilization of renewable agricultural residues for the production of extracellular halostable cellulase from newly isolated Halomonas sp. strain PS47

A newly isolated biopolymer-degrading halophilic bacterium, Halomonas sp. strain PS47, yielded higher cellulase activity (0.0076 U/ml) in mineral salt medium (MM63). Activity increased to 0.029 U/ml when carboxymethyl cellulose (0.5 % w/v) was used as carbon source and further to 0.138 U/ml when a combination of yeast extract and peptone was used as nitrogen source. Enzyme secretion was maximal during late exponential and stationary phases (0.15 U/ml, 48 h). Among different agro-residues (1 % w/v), wheat bran gave the highest activity (0.12 U/ml) at pH 7.5, 30 °C and 6 % (w/v) NaCl. The cellulase exhibited higher activity at pH 7.1 and 50 °C. The enzyme exhibited activity over a wide range of NaCl concentrations (0–4 M). Optimum activity was at 0–1 M NaCl. At 4 M NaCl, activity was reduced to 65 % of the initial value. The present investigation thus contributes to the limited information available on halostable cellulases.     

Front-end recovery of protein from lignocellulosic biomass and its effects on chemical pretreatment and enzymatic saccharification

Front-end protein recovery from biomass at different maturities, and its effects on chemical pretreatment and enzyme hydrolysis of partially deproteinized fiber were investigated. The protein recovery from alfalfa and switchgrass biomass using sodium dodecyl sulfate and potassium hydroxide treatments was ~50–65 % of initial biomass protein. When hot water was used as extraction media, the protein recovery was 52.9 and 43.7 % of total protein in switchgrass and alfalfa, respectively. For any treatment, relative protein recovery was higher from switchgrass than from alfalfa. Only approximately half the total protein was recovered from relatively mature (early fall) biomass compared with midsummer harvested biomass. When protein was recovered partially using sodium dodecyl sulfate or potassium hydroxide, and leftover fiber pretreated, aqueous ammonia pretreatment removed 58.5–60.1 % of lignin and retained more cellulose in the fiber compared with acid pretreatment (nearly no lignin removal). Protein removal was helpful in the enzyme digestibility of fibers. Delignification of ammonia pretreated partially deproteinized alfalfa fiber was in the range of 34.4–45 %, while dilute sulfuric acid did not remove lignin effectively. Overall, the higher delignification and enzyme digestibilities were observed in aqueous ammonia pretreated partially deproteinized alfalfa fibers regardless of biomass type.     

Enzymatic Saccharification of Lignocelluloses Should be Conducted at Elevated pH 5.2–6.2

This study revealed that cellulose enzymatic saccharification response curves of lignocellulosic substrates were very different from those of pure cellulosic substrates in terms of optimal pH and pH operating window. The maximal enzymatic cellulose saccharification of lignocellulosic substrates occurs at substrate suspension pH 5.2–6.2, not between pH 4.8 and 5.0 as exclusively used in literature using T. reesi cellulase. Two commercial cellulase enzyme cocktails, Celluclast 1.5L and CTec2 both from Novozymes, were evaluated over a wide range of pH. The optimal ranges of measured suspension pH of 5.2–5.7 for Celluclast 1.5L and 5.5–6.2 for CTec2 were obtained using six lignocellulosic substrates produced by dilute acid, alkaline, and two sulfite pretreatments to overcome recalcitrance of lignocelluloses (SPORL) pretreatments using both a softwood and a hardwood. Furthermore, cellulose saccharification efficiency of a SPORL-pretreated lodgepole pine substrate showed a very steep increase between pH 4.7 and 5.2. Saccharification efficiency can be increased by 80 % at cellulase loading of 11.3 FPU/g glucan, i.e., from approximately 43 to 78 % simply by increasing the substrate suspension pH from 4.7 to 5.2 (buffer solution pH from 4.8 to 5.5) using Celluclast 1.5L, or by 70 % from approximately 51 to 87 % when substrate suspension pH is increased from 4.9 to 6.2 (buffer solution pH from 5.0 to 6.5) using CTec2. The enzymatic cellulose saccharification response to pH is correlated to the degree of substrate lignin sulfonation. The difference in pH-induced lignin surface charge, and therefore surface hydrophilicity and lignin–cellulase electrostatic interactions, among different substrates with different lignin content and structure is responsible for the reported different enhancements in lignocellulose saccharification at elevated pH.     

OPTIMIZATION OF AFFINITY DIGESTION FOR THE ISOLATION OF CELLULOSOMES FROM Clostridium thermocellum

The affinity digestion process for cellulase purification consisting of binding to amorphous cellulose, and amorphous cellulose hydrolysis in the presence of dialysis (Morag et al., 1991), was optimized to obtain high activity recoveries and consistent protein recoveries in the isolation of Clostridium thermocellum cellulase. Experiments were conducted using crude supernatant prepared from C. thermocellum grown on either Avicel or cellobiose. While no difference was observed between Avicel-grown or cellobiose-grown cellulase in the adsorption step, differences were observed during the hydrolysis step. The optimal amorphous cellulose loading was found to be 3 mg amorphous cellulose per milligram supernatant protein. At this loading, 90–100% of activity in the crude supernatant was adsorbed. Twenty-four-hour incubation with the amorphous cellulose during the adsorption stage was found to result in maximal and stable adsorption of activity to the substrate. By fitting the adsorption data to the Langmuir model, an adsorption constant of 410 L/g and a binding capacity of 0.249 g cellulase/g cellulose were obtained. The optimal length of time for hydrolysis was found to be 3 hr for cellulase purified from Avicel cultures and 4 hr for cellulase purified from cellobiose cultures. These loadings and incubation times allowed for more than 85% activity recovery.     

Effect of Urea on the Enzymatic Hydrolysis of Lignocellulosic Substrate and Its Mechanism

Effect of hydrogen bond breaker (urea) addition on the enzymatic hydrolysis of Avicel and eucalyptus pretreated by dilute acid (Eu-DA) was investigated. Urea enhanced the enzymatic hydrolysis of Eu-DA at 50 or 30 °C when the concentration of urea was below 60 g/L, while it inhibited the hydrolysis of Avicel. Low concentration urea (<?240 g/L) had little effect on the cellulase spatial structure and its activity. But it decreased cellulase binding to cellulose surface to inhibit the cellulose hydrolysis. Meanwhile, urea obviously prevented the adsorption of cellobiohydrolase I (CBHI) on the lignin in spite of little effect on the adsorption of β-glucosidase (BGL) and two endoglucanases (EGIII and EGV) on lignin. It was proposed that urea enhanced the enzymatic efficiency of Eu-DA by decreasing the cellulase adsorption on lignin surface.     

The Role of Polymeric Micelles on Chemical Changes of Pretreated Corn Stover,Cellulase Structure,and Adsorption

Enzymatic hydrolysis of lignocellulosic biomass is limited by rapid cellulase deactivation, consequently requiring large amounts of enzyme to maintain acceptable biomass conversion. In this study, a new approach to improve lignocellulose hydrolysis was investigated. Performing enzymatic hydrolysis of corn stover (CS) in the presence of polymeric–surfactant micelles (PMs) was demonstrated to improve hydrolysis yield to a greater extent than using only surfactant micelles. Application of 2 % (w/w) of polyethylene glycol (PEG 6000) with casein, Tween-20, and Triton X-100 at levels above the critical micelle concentrations increased the hydrolysis yield of CS containing high-bound lignin (extrusion-pretreated) by up to 87.8, 11.7, and 7.5 %, respectively. These PMs were not effective during enzymatic hydrolysis of biomass lacking lignin (Avicel) or alkali-pretreated CS (7.2 % lignin). The main reasons for the enhanced cellulase activity observed due to PEG-casein, PEG-Tween, and PEG-Triton were enhanced cellulase solubilization; reformation of α-helix substructure; and combination of induced cellulase solubilization, α-helix reformation, and chemical changes in the microstructure of biomass, respectively. Deformation of the cellulase substructure during hydrolysis of biomass and its subsequent reformation in the presence of surfactants were shown in this study for the first time. Chemical changes in the microstructure of biomass (e.g., lignin side changes, C–O bonds, and amorphous cellulose) were found to be another potential reason for the effectiveness of surfactants when they are incubated at above 6 g/L for 72 h with biomass.     

Characterization of Clostridium thermocellum Isolates Grown on Cellulose and Sugarcane Bagasse

Although plant cell walls may be degraded by microbial free enzymes, many bacteria degrade cellulose via enzyme complexes called cellulosomes. The study of the structures and mechanisms of these large macromolecular complexes is an active and ongoing research topic, with the goal of developing methods to improve lignocellulosic biomass conversion using cellulosomes. The aim of the present work was to evaluate and characterize the holocellulolytic activities produced by two new isolates (ISO1 and ISO2) of the spore-forming thermophilic anaerobic bacterium Clostridium thermocellum, during growth on crystalline cellulose and sugarcane bagasse, in comparison with activities obtained from the C. thermocellum strain CthJW. The pH and temperature values for optimal growth of the isolates were pH 7 and 60 °C, respectively. The isolates produced cellulolytic, xylanolytic, and pectinolytic activities when cultured on crystalline cellulose or sugarcane bagasse, which have never been used previously as the sole carbon source for these bacteria. The profiles of secreted proteins for these isolates, ISO1 and ISO2, were quite different from those obtained for the standard strain CthJW and from each other, as shown by 2D gel electrophoresis maps, and these profiles also depend on the carbon source used. Different protein isoforms were also detected in the maps for all growth conditions and bacterial strains. MALDI-TOF mass spectrometry was used to identify the differentially expressed proteins for ISO1 and ISO2 under growth in the presence of cellulose as carbon source. Twenty-five differentially expressed spots were identified and grouped into 8 functional categories: metabolism (20 %), motor function (20 %), protein synthesis (12 %), oxidative stress (16 %), secretory pathway (12 %), cellulose hydrolysis (4 %), protein folding (4 %), and defense (12 %). Spots 200 and 197, identified as a glycosyl hydrolase family member 9 and as a chaperone GroEL, respectively, were detected for all isolates and are potentially related to cellulosome architecture.     

The effect of isolated lignins,obtained from a range of pretreated lignocellulosic substrates,on enzymatic hydrolysis

The influence of the residual lignin remaining in the cellulosic rich component of pretreated lignocellulosic substrates on subsequent enzymatic hydrolysis was assessed. Twelve lignin preparations were isolated by two isolation methods (protease treated lignin (PTL) and cellulolytic enzymatic lignin (CEL)) from three types of biomass (corn stover, poplar, and lodgepole pine) that had been pretreated by two processes (steam and organosolv pretreatments). Comparative analysis of the isolated lignin showed that the CEL contained lower amounts of carbohydrates and protein than did the PTL and that the isolated lignin from corn stover contained more carbohydrates than did the lignin derived from the poplar and lodgepole pine. The lower yields of acid insoluble lignin (AIL) obtained from the corn stover when using the PTL method indicated that the lignin from the corn stover had a higher hydrophilicity than did the lignin from the poplar and lodgepole pine. The isolated lignin preparations were added to the reaction mixture containing crystalline cellulose (Avicel) and their possible effects on enzymatic hydrolysis were assessed. It was apparent that the lignin isolated from lodgepole pine and steam pretreated poplar decreased the hydrolysis yields of Avicel, whereas the other isolated lignins did not appear to decrease the hydrolysis yields significantly. The hydrolysis yields of the pretreated lignocellulose and those of Avicel containing the PTL showed good correlation, indicating that the nature of the residual lignin obtained after pretreatment significantly influenced hydrolysis. Biotechnol. Bioeng. 2010;105: 871–879. © 2009 Wiley Periodicals, Inc.