Automated filter paper assay for determination of cellulase activity

Recent developments in molecular breeding and directed evolution have promised great developments in industrial enzymes as demonstrated by exponential improvements in β-lactamase and green fluorescent protein (GFP). Detection of and screening for improved enzymes are relatively easy if the target enzyme is expressible in a suitable high-throughput screening host and a clearly defined and usable screen or selection is available, as with GFP and β-lactamase. Fungal cellulases, however, are difficult to measure and have limited expressibility in heterologous hosts. Furthermore, traditional cellulase assays are tedious and time-consuming. Multiple enzyme components, an insoluble substrate, and generally slow reaction rates have plagued cellulase researchers interested in creating cellulase mixtures with increased activities and/or enhanced biochemical properties. Although the International Union of Pure and Applied Chemists standard measure of cellulase activity, the filter paper assay (FPA), can be reproduced in most laboratories with some effort, this method has long been recognized for its complexity and susceptibility to operator error. Our current automated FPA method is based on a Cyberlabs C400 robotics deck equipped with customized incubation, reagent storage, and plate-reading capabilities that allow rapid evaluation of cellulases acting on cellulose and has a maximum throughput of 84 enzyme samples per day when performing the automated FPA.     

Cellulase retention and sugar removal by membrane ultrafiltration during lignocellulosic biomass hydrolysis

Technologies suitable for the separation and reuse of cellulase enzymes during the enzymatic saccharification of pretreated corn stover are investigated to examine the economic and technical viability of processes that promote cellulase reuse while removing inhibitory reaction products such as glucose and cellobiose. The simplest and most suitable separation is a filter with relatively large pores on the order of 20–25 mm that retains residual corn stover solids while passing reaction products such as glucose and cellobiose to form a sugar stream for a variety of end uses. Such a simple separation is effective because cellulase remains bound to the residual solids. Ultrafiltration using 50-kDa polyethersulfone membranes to recover cellulase enzymes in solution was shown not to enhance further the saccharification rate or overall conversion. Instead, it appears that the necessary cellulase enzymes, including β-glucosidase, are tightly bound to the substrate; when fresh corn stover is contacted with highly washed residual solids, without the addition of fresh enzymes, glucose is generated at a high rate. When filtration was applied multiple times, the concentration of inhibitory reaction products such as glucose and cellobiose was reduced from 70 to 10 g/L. However, an enhanced saccharification performance was not observed, most likely because the concentration of the inhibitory products remained too high. Further reduction in the product concentration was not investigated, because it would make the reaction unnecessarily complex and result in a product stream that is much too dilute to be useful. Finally, an economic analysis shows that reuse of cellulase can reduce glucose production costs, especially when the enzyme price is high. The most economic performance is shown to occur when the cellulase enzyme is reused and a small amount of fresh enzyme is added after each separation step to replace lost or deactivated enzyme.     

Stability and recovery ofPenicillium funiculosum cellulase under use conditions

The stability ofPenicillium funiculosum cellulase has been investigated under the conditions used for cellulose hydrolysis. Fifty five percent of filter paper activity (FPA) was inactivated on incubation at 50°C for 24 h, whereas there was no loss in endoglucanase and β-glucosidase activity. The addition of 2% polyethylene glycol (PEG) during incubation stabilized the FPA. The influence of pH during fermentation on the thermal stability of the enzyme is discussed. The recovery of enzymes after hydrolysis of bagasse at 50°C was between 8 and 14%. Under the optimal conditions of elution, the recovery of enzyme was 35% (1). Increasing the enzyme to the substrate ratio fivefold and presence of PEG during hydrolysis resulted in 80, 83, and 95% recovery of β-glucosidase, FPA, and endoglucanase activity, respectively. Index Entries: Stability; recovery of cellulase P.funiculosum.     

A study on the inhibition of cellulolytic activities by lignin

It is well known that cellulolytic enzymes hardly attack lignocellulose. Hitherto knowledge, however, has not yet fully elucidated the mechanisms of the inhibition; whether it depends on a steric hindrance or protein-binding inhibition. For the purpose of acceleration of enzymatic digestion of lignocellulose biomass, the study was carried out using partially purified cellulase of Meicelase and milled wood lignin from soft or hard wood. Milled wood lignin was prepared from soft wood,Picea jezoensis, or from hard wood,Quercus serrata, by the method of Björkman. Lignin was dissolved in methyl cellosolve, since the solvent has little effect on cellulolytic activities, and enzymic activities were followed with partially purified Meicelase. The results show that cellobiose activities of enzymes fromTrichoderma viride are markedly depressed by both lignin of soft and hard wood, and the former lignin inhibits the reaction stronger than the latter. Lignins show no inhibition in the reaction with CMC and debris of filter paper. Liberation of glucose from filter paper by the enzyme in the presence of lignin is also depressed, and addition of cellobiase instead of lignin in the above enzyme reaction shows the delay of time for breakdown of filter paper. This phenomenon indicates that lignin inhibits enzymic decomposition of cellobiose in the degradation pathway of cellulose and accumulated cellobiose gives a feedback function to digestion of fibers of paper.     

Use of a new membrane-reactor saccharification assay to evaluate the performance of celluloses under simulated ssf conditions

A new saccharification assay has been devised, in which a continuously buffer-swept membrane reactor is used to remove the solubilized saccharification products, thus allowing high extents of substrate conversion without significant inhibitory effects from the buildup of either cellobiose or glucose. This diafiltration saccharification assay (DSA) can, therefore, be used to obtain direct measurements of the performance of combinations of cellulase and substrate under simulated SSF conditions, without the saccharification results being complicated by factors that may influence the subsequent fermentation step. This assay has been used to compare the effectiveness of commercial and special in-house-producedTrichoderma reeSci. cellulase preparations in the saccharification of a standardized microcrystalline (Sigmacell) substrate and a dilute-acid pretreated lignocellulosic substrate. Initial results strongly suggest that enzyme preparations produced in the presence of the targeted lignocellulosic substrate will saccharify that substrate more effectively. These results call into question the widespread use of the “filter paper assay” as a reliable predictor of enzyme performance in the extensive hydrolysis of substrates that are quite different from filter paper in both physical properties and chemical composition.

     

Enhanced glucose production from cellulose using coimmobilized cellulase and β-glucosidase

β-Glucosidase was covalently immobilized alone and coimmobilized with cellulase using a hydrophilic polyurethane foam (Hypol®FHP 2002). Immobilization improved the functional properties of the enzymes. When immobilized alone, the K_m for cellobiose of β-glucosidase was decreased by 33% and the pH optimum shifted to a slightly more basic value, compared to the free enzyme. Immobilized β-glucosidase was extremely stable (95% of activity remained after 1000 h of continuous use). Coimmobilization of cellulase and β-glucosidase produced a cellulose-hydrolyzing complex with a 2.5-fold greater rate of glucose production for soluble cellulose and a four-fold greater increase for insoluble cellulose, compared to immobilized cellulase alone. The immobilized enzymes showed a broader acceptance of various types of insoluble cellulose substrates than did the free enzymes and showed a long-term (at least 24 h) linear rate of glucose production from microcrystalline cellulose. The pH optimum for the coimmobilized enzymes was 6.0. This method for enzyme immobilization is fast, irreversible, and does not require harsh conditions. The enhanced glucose yields obtained indicate that this method may prove useful for commercial cellulose hydrolysis.     

Use of Cellulase Inhibitors to Produce Cellobiose

The economics driving biorefinery development requires high value-added products such as cellobiose for financial feasibility. This research describes a simple technology for increasing cellobiose yields during lignocellulosic hydrolysis. The yield of cellobiose produced during cellulose hydrolysis was maximized by modification of reaction conditions. The addition of an inhibitor from the group that includes glucose oxidase, gluconolactone, and gluconic acid during cellulase hydrolysis of cellulose increased the amount of cellobiose produced. The optimal conditions for cellobiose production were determined for four factors; reaction time, cellulase concentration, cellulose concentration, and inhibitor concentration using a Box-Behnken experimental design. Gluconolactone in the cellulase system resulted in the greatest production of cellobiose (31.2%) from cellulose. The yield of cellobiose was 23.7% with glucose oxidase, similar to 21.9% with gluconic acid.     

Enhanced Enzymatic Hydrolysis of Lignocellulose by Optimizing Enzyme Complexes

To enhance the conversion of the cellulose and hemicellulose, the corncob pretreated by aqueous ammonia soaking was hydrolyzed by enzyme complexes. The saturation limit for cellulase (Spezyme CP) was determined as 15 mg protein/g glucan (50 filter paper unit (FPU)/g glucan). The accessory enzymes (β-glucosidase, xylanase, and pectinase) were supplemented to hydrolyze cellobiose (cellulase-inhibiting product), hemicellulose, and pectin (the component covering the fiber surfaces), respectively. It was found that β-glucosidase (Novozyme 188) loading of 1.45 mg protein/g glucan [30 cellobiase units (CBU)/g glucan] was enough to eliminate the cellobiose inhibitor, and 2.9 mg protein/g glucan (60 CBU/g glucan) was the saturation limit. The supplementation of xylanase and pectinase can increase the conversion of cellulose and hemicellulose significantly. The yields of glucose and xylose enhanced with the increasing enzyme loading, but the increasing trend became low at high loading. Compared with xylanase, pectinase was more effective to promote the hydrolysis of cellulose and hemicellulose. The supplementation of pectinase with 0.12 mg protein/g glucan could increase the yields of glucose and xylose by 7.5% and 29.3%, respectively.     

An easy and practical method for detection and estimation of microcrystalline cellulose in pasteurized milk

Microcrystalline cellulose (MCC) is suspected to be a new adulteration in pasteurized milk in China, yet an efficient method for MCC detection in dairy has not been established. This study presents a novel procedure to detect and estimate MCC in pasteurized milk using dialysis, cellulase hydrolysis, and a reducing sugar assay. The background value of reducing sugar was eliminated by dialysis, and cellulase activity toward MCC was stable in dialyzed milk. A criterion for MCC detection and an empirical formula for MCC estimation were summarized based on the reducing sugar variation after hydrolysis. The detection sensitivity was below 0.5 g/L. Reducing sugar distribution after cellulase-catalyzed hydrolysis was examined by HPLC, and revealed that most of the detected sugar was glucose. This paper describes a practical method for detection of MCC in pasteurized milk that might benefit dairy QC.     

Fast and simple glucose assay based on filter paper as enzymes carrier using phone camera detection

Glucose is a typical diagnostic marker of diabetes mellitus but it may be also helpful during diagnosis of some types of poisoning, immunological disorder or long-term stress at hospitalized patients. Diagnosis of diabetes mellitus in time is indispensable for prevention of life-threatening complication and so, accurate and easy device for non-invasive and accurate self-diagnosis is necessary. Simple assay based on filter paper with chitosan layer and with immobilized enzymes glucose oxidase and peroxidase and phone camera detection has been proposed for home-care glucose detection in urine. Data were processed in RGB (red–green–blue) color model when blue color channel showed the best sensitivity to changing glucose concentrations. Assay exerted linear regression from 0 to 4 mmol/l and limit of detection was set to be 166 µmol/l. Assay was not influenced by any interfering substances including maltose, sucrose, sorbitol or fructose or by urine matrix substance such as bovine serum albumin, ascorbic acid, uric acid or urea. Measurement of glucose from spiked urine samples reveals also no influence of the matrix on the assay. Long-term stability was measured and filter papers coated by enzymes showed excellent stability for at least 9 weeks without any special treatment or package. In comparison with differently modified filter paper, filter paper with both chitosan and enzymes showed the best sensitivity to changing glucose concentration. In a conclusion, simple (phone camera detection) and fast (3-min reaction) assay for quantitative detection of glucose from urine was optimized.     

Determination by the enzyme thermistor of cellobiose formed on degradation of cellulose

A calorimetric assay procedure for the determination of cellobiose has been developed. The cellobiose is hydrolyzed by β-glucosidase and the glucose formed is measured calorimetrically by an enzyme thermistor containing co-immobilized glucose oxidase and catalase. The system was optimized with regard to the arrangement of the enzymes, the pH-dependence of the separate enzymic steps, and of the total system. By placing the β-glucosidase in a precolumn that could be switched in and out of the flow through the enzyme thermistor, both cellobiose and glucose present in the sample could be determined. The performance with standard solutions and with crude samples from cellulose degradation experiments was investigated.     

TheTalaromyces emersonii enzyme system

In typical fermentations at 45‡C on cellulose/corn steep liquor/ammonium and mineral salts medium, growth of the thermophilic fungusTalaromyces emersonii increases rapidly up to about 50 h and then decreases, presumably because of cell lysis, sporulation, or both. The accumulation of cellulase activity follows closely on growth and essentially reaches a maximum at about the same time that cell protein does. By contrast, two peaks of Β-glucosidase activity are observed, one maximal at about 36 h and the second at about 75 h. Fractionation of culture filtrates showed that the cellulase system is comprised of at least four endoglucanases (EC 3.2.1.4), four or five exoglucanases (cello-biohydrolase; EC 3.2.1.91), and three types of Β-glucosidase (cellobiase; EC 3.2.1.21). All are glycoproteins. Indeed, variation in carbohydrate content may account for some of the observed multiplicity of enzyme forms. Although none of the individual components is active against cellulose, reconstitution experiments show that appropriate mixtures of each type act synergistically to effect hydrolysis of substrate. In addition to the three extracellular Β-glucosidases I (M_r, 135,000), II (M_r, 100,000), and III (M_r, 45,700), an intracellular form, IV (M_r, 57,600), has been isolated. All exist as single polypeptides. The extracellular forms I and III are most active at 70‡C, pH 5, and have half-lives under these conditions of 6 and 3 h, respectively. By contrast, the intracellular form (IV) is most active at 35‡C and is rapidly denatured at higher temperatures. Substrate specificity and other studies provide clues to their possible roles in vivo. Β-Glucosidase III acts as an exoglucohydrolase by removing glucose residues from cellooligosaccharides arising from the action of endocellulases. Β-Glucosidase I is the major enzyme involved in cleaving cellobiose and short chain cellooligosaccharides. In doing so it relieves the inhibition by cellobiose of cellulase action. The intracellular form, Β-glucosidase IV, may have a dual role. By virtue of its transferase activity it may convert incoming cellobiose to the active inducer of cellulase synthesis, whereas by cleaving cellobiose to glucose (hydrolase action) it provides energy for the cell and a repressor of cellulase formation. Four endocellulases have been purified to apparent homogeneity as judged by electrophoresis. Preliminary results show that they all have M_r values of about 70,000 and pI values less than 4. However, they differ from one another in carbohydrate content, thermal stability, and affinity for substrate. The complete cellulase system is most active at pH 4.2, 60–65‡C, and retains about 80% of its original activity after 5 d incubation at 60‡C, pH 5. Avicel and filter paper most effectively induce synthesis of the complete cellulase system, as measured by the ability of culture filtrate to digest filter paper. Cotton, Solka floc, and α-cellulose are also effective inducers, as are “wastes” such as newspaper, straw, and beet pulp. Little or no cellulase synthesis is evident when lactose, cellobiose, or glucose replaces cellulose in growth media. From a practical viewpoint we find that saccharification of beet pulp is most readily achieved by using enzyme (i.e., culture filtrate) obtained by growing the organism on medium containing beet pulp as the source of cellulose. Of the various strains ofTalaromyces emersonii investigated for cellulase production, we found CBS 814.70 to be the best, yielding approx. 0.5 IU/mL of culture filtrate. By medium optimization and genetic manipulation we have isolated a number of mutants of this strain giving 2 IU/mL or more and enzyme productivities of 20–25 IU/L/h. Xylanase, arabinogalactanase, and pectinase activities have also been detected in culture filtrates of the organism when grown on beet pulp. Various lignocellulosic materials, including cotton, Solka floc, Avicel, filter paper, newspaper, and straw, can be degraded by the enzyme system. However, much of our effort has been directed to investigation of the saccharification of beet pulp since it is available in large quantities at central locations and because its lignin content is low. About 85% of the dry weight of this material is accounted for by cellulose, hemicellulose, and pectin in roughly equal proportions. Culture filtrates effect significant saccharification of pulp as measured by the release of reducing sugars or of glucose. Ball-milling the pulp prior to incubation with enzyme effects considerable improvement in the extent of digestion. Alkali or peracetic acid pretreatment of the ball-milled substrate facilitates enzymic hydrolysis even further. Good results are also obtained when unmilled pulp is (a) pretreated with pectinase prior to incubation with normal culture filtrates or (b) incubated with more concentrated culture filtrates with good pectinase activity. Under suitable conditions, 80% hydrolysis of beet pulp polysaccharides was achieved in 5 d at 60‡C, pH 5.     

Production, purification, and biochemical characterization of two beta-glucosidases from Sclerotinia sclerotiorum

The filamentous fungus Sclerotinia sclerotiorum produces beta-glucosidases in liquid culture with a variety of carbon sources, including cellulose (filter paper), xylan, barley straw, oat meal, and xylose. Analysis by native polyacrylamide gel electrophoresis (PAGE) followed by an activity staining with the specific chromogenic substrate, 5-bromo 4-chloro 3-indolyl beta-1,4 glucoside (X-glu) showed that two extracellular beta-glucosidases, designated as beta-glu1 and beta-glu2, were in the filter paper culture filtrate. Only one enzyme designated as beta-glu x was revealed by the same method in the xylose culture filtrate. Beta-glu1 and beta-glu2 were purified to homogeneity. The purification procedure consist of a common step of anion-exchange chromatography on DEAE-Sepharose CL6B, both high-performance liquid chromatography (HPLC) anion-exchange and gel filtration columns for beta-glu1 and only HPLC gel filtration for beta-glu2. Beta-glu1 has a molecular mass of 196 kDa and 96.5 kDa, as estimated by gel filtration and sodium dodecyl sulfate (SDS)-PAGE, respectively, suggesting that the native enzyme may consist of two identical subunits. The same analysis showed that beta-glu2 is a monomeric protein with an apparent molecular mass of about 76.5 kDa. Beta-glu1 and beta-glu2 hydrolyses PNPGlc and cellobiose, with apparent Km values respectively for PNPGlc and cellobiose of 0.1 and 1.9 mM for beta-glu1 and 2.8 and 8 mM for beta-glu2. Both enzymes exhibit the same temperature and pH optima for PNPGlc hydrolysis (60 degrees C and pH 5.0). beta-glu1 was stable over a pH range of 3-8 and kept 50% of its activity after 30 min of heating at 60 degrees C without substrate. It was further characterized by studying the effect of some cations and various reagents on its activity.     

Sampling, dilution, and loading device-coupled high-performance liquid chromatography method for successive on-line analyses of major carbohydrate products in immobilized cellulase hydrolysate of paper cellulose.

A device with direct sampling, dilution, and sample loading has been utilized to couple a vertically hanging immobilized cellulase bioreactor with a high-performance liquid chromatography system to make a successful on-line analysis of the 3 major carbohydrate products: glucose, xylose, and cellobiose in the cellulase hydrolysate. The coupled analysis system for successive on-line monitoring of the enzymatic hydrolysis of paper cellulose was stable over a period of 96 h. A comparative study involving 4 different quantification methods for the 3 carbohydrates was conducted. The internal standard calibration method with on-line dilution was observed to be the best procedure in terms of accuracy, precision, limit of detection, and systematic error reduction. With this method, the analysis for glucose had 99.9% accuracy, RSD below 2.4%, and a 2.1 ppm detection limit. Matrix matching was found important in the preparation of standard calibration curves with refractive index detection.     

A Study of the Hydrolysis of Waste Paper Cellulose with a Vertically Hanging Immobilized Cellulase Reactor and the Reuse of the Immobilized Cellulase

A commercialized cellulase from Trichoderma reesei has been successfully immobilized by using calcium alginate gel in our laboratory. The waste paper cellulose was hydrolyzed with a special design of the reactor to form a vertically hanging immobilized cellulase under the optimum conditions of pH 4.0 and 45 °C. Glucose, cellobiose and xylose are the major hydrolysis products. The glucose production from the hydrolysis with the vertically hanging immobilized cellulase was about 1.73‐fold better than the freely suspended immobilized cellulase. The average diameter of the immobilized cellulase pellets was 4.190 ± 0.291 mm. UV light irradiation deactivates the activity of the immobilized cellulase. The advantage of the vertically hanging immobilized cellulase reactor is an easy recycle and reuse of the immobilized cellulase. Washing and soaking the recycled immobilized cellulase with distilled water for one day can restore its activity to a small extent. Overall, the application of the hanging immobilized cellulase reactor for waste paper cellulose hydrolysis is successful.     

Pretreatment of sugar cane bagasse hemicellulose hydrolyzate for ethanol production by yeast

The cellulase system ofBacillus circulans F-2 effectively hydrolyzed carboxymethyl cellulose (CMC), xylan, avicel, cellobiose, filter paper, cotton, andp-nitrophenyl-Β-D-cellobioside, and the crude enzyme produced mainly glucose from digestion of avicel. Two major and one minor peaks of enzyme activities were eluted on DEAE ion-exchange chromatography, and designated cellulase complex I(C-I) and complex II(C-II) for the two major peaks, and cellulase-III for a minor peak. C-I and C-II were further purified on gel filtration column of a TSK-Gel SW G3000 ×L. The molecular masses of C-I and C-II were estimated to be about 669 and 443 kDa, respectively. Sodium dodecyl sulfate-polyacrylamide gel electrophoretic analysis of the C-I and C-II complexes showed that the C-I complex was present as a multiple protein complex, consisting of at least five CMCases and two xylanases, and that the C-II complex was consisted of at least three CMCase and four xylan ases. C-I showed high activities of cellohydrolase, CMCase, xylanase, and Β-glucosidase, whereas C-II showed high activities of CMCase, xylanase, avicelase, and Β-glucosidase. The outstanding property of the C-II was its high hydrolytic activity toward filter paper, a highly resistant substrate against enzymatic degradation. However, cellulaseIII showed only strong avicelase activity. These results indicated that the cellulase system of the strain exists as multiple complex forms.     

Enhancing enzymatic hydrolysis of crystalline cellulose and lignocellulose by adding long-chain fatty alcohols

The effects of long-chain fatty alcohols (LFAs) on the enzymatic hydrolysis of crystalline cellulose by two commercial Trichoderma reesei cellulase cocktails (CTec2 and Celluclast 1.5L) were studied. It was found that n-butanol inhibited the enzymatic hydrolysis, but n-octanol, n-decanol and n-dodecanol had strong enhancement on enzymatic hydrolysis of crystalline cellulose in the buffer pH range from 4.0 to 6.0. LFAs can increase the hydrolysis efficiency of crystalline cellulose from 37 to 57 % at Celluclast 1.5L loading of ten filter paper units (FPU)/g glucan. LFAs have similar enhancement on the enzymatic hydrolysis of crystalline cellulose mixed with lignin or xylan. The enhancement of LFAs increased with the decrease of the crystallinity index. LFAs not only enhanced the high-solid enzymatic hydrolysis of lignocellulose, but also improved the rheological properties of high-solid lignocellulosic slurries by decreasing the yield stress and complex viscosity. Meanwhile, LFAs can improve the enzymatic hydrolysis of cellobiose to glucose, especially at low cellulase loading.     

Enhancement of enzymatic cellulose hydrolysis using a novel type of bioreactor with intensive stirring induced by electromagnetic field

The use of the intensive mass transfer reactor (IMTR) for enzymatic saccharification of cellulose, where the reaction mixture is intensively stirred by ferromagnetic particles (FMP), enhances the process rate and productivity drastically. The most significant enhancement of the process was observed when microcrystalline cellulose was used as a substrate. A concentration of sugars up to 5% was obtained after 1 h of cellulose hydrolysis using a cellulase activity level of 2 filter paper units (FPU)/mL (20 FPU/g substrate). In the hydrolysis of two types of industrial cellulosic wastes, the enhancement effects were less pronounced. Parameters related to the IMTR design, such as the shape, dimensions, and mass of FMP, as well as the magnetic field strength, strongly affected the process of hydrolysis. Among various kinds of FMP tested, the most efficient were found to be cylindrical particles (0.25 x 4 mm). In general, the hydrolysis rate enhanced when the magnetic field strength increased from 26,000 to 64,000 A/m. An optimal FMP loading existed at each level of the field strength. Hydrolyzates obtained in the IMTR under the action ofTrichoderma reesei andPenicillium verruculosum cellulases contained glucose and cellobiose as soluble products, cellobiose being predominant (> 50%). Only when a high level of extra Β-glucosidase was added to the IMTR (10 CBU/mL), did glucose made up more than 90% of the products. Owing to extreme shear conditions in the IMTR, significant enzyme inactivation took place.     

Production of cellulase/β-glucosidase by the mixed fungi culture of Trichoderma reesei and Aspergillus phoenicis on dairy manure

A cellulase production process was developed by growing the fungi Trichoderma reesei and Aspergillus phoenicis on dairy manure. T. reesei produced a high total cellulase titer (1.7 filter paper units [FPU]/mL, filter paper activity) in medium containing 10 g/L of manure (dry basis [w/w]), 2 g/L KH₂PO₄, 2 mL/L of Tween-80, and 2mg/L of CoCl₂. However, β-glucosidase activity in the T. reesei-enzyme system was very low. T. reesei was then cocultured with A. phoenicis to enhance the β-glucosidase level. The mixed culture resulted in a relatively high level of total cellulase (1.54 FPU/mL) and β-glucosidase (0.64 IU/mL). The ratio of β-glucosidase activity to filter paper activity was 0.41, suitable for hydrolyzing manure cellulose. The crude enzyme broth from the mixed culture was used for hydrolyzing the manure cellulose, and the produced glucose was significantly (p<0.01) higher than levels obtained by using the commercial enzyme or the enzyme broth of the pure culture T. reesei.     

Effects of sugar inhibition on cellulases and β-glucosidase during enzymatic hydrolysis of softwood substrates

A quantitative approach was taken to determine the inhibition effects of glucose and other sugar monomers during cellulase and β-Glucosidase hydrolysis of two types of cellulosic material: Avicel and acetic acid-pretreated softwood. The increased glucose content in the hydrolysate resulted in a dramatic increase in the degrees of inhibition on both β-Glucosidase and cellulase activities. Supplementation of mannose, xylose, and galactose during cellobiose hydrolysis did not show any inhibitory effects on β-Glucosidase activity. However, these sugars were shown to have significant inhibitory effects on cellulase activity during cellulose hydrolysis. Our study suggests that high-substrate consistency hydrolysis with supplementation of hemicellulose is likely to be a practical solution to minimizing end-product inhibition effects while producing hydrolysate with high glucose concentration.