Lignocellulose biotransformation with immobilized cellulase,d-glucose oxidase and fungal peroxidases

Three enzymes, cellulase [see 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4], d-glucose oxidase (β-d-glucose: oxygen 1-oxidoreductase, EC 1.1.3.4) and peroxidase (donor:hydrogen peroxide oxidoreductase, EC 1.11.1.7) immobilized on glass beads, have been incubated with lignocellulose. Fungal peroxidases from Trametes versicolor and Inonotus radiatus when mixed with cellulase and d-glucose oxidase were able to liberate phenolic compounds and d-glucose from lignocellulose. Three lignin monomers were identified. When the immobilized enzymes were incubated individually with lignocellulose they did not degrade lignin.     

Production of xylanolytic enzymes in association with the cellulolytic activities of Penicillium funiculosum

Penicillium funiculosum produced 16 and 0.4 units ml^?1 of d-xylanase (1,4-β-d-xylan xylanohydrolase, EC 3.2.1.8) and β-d-xylosidase (1,4-β-d-xylan xylohydrolase, EC 3.2.1.37), respectively, in shake flasks. Both enzymes were 100% stable when heated at 50°C for 30 min and on prolonged heating d-xylanase and β-d-xylosidase showed 46 and 20% loss, respectively. Maximum hydrolysis (75%) of d-xylan was obtained when the end products were removed. The addition of β-d-xylosidase markedly influenced the degree of hydrolysis of d-xylan. End-product analysis of the d-xylan hydrolysate showed the presence of d-xylose, d-xylobiose, d-xylotriose, d-xylotetraose, d-xylopentose and l-arabinose. The fractionation of culture filtrate of Penicillium funiculosum grown on cellulose powder or in a combination of cellulose powder and wheat bran indicated the presence of two d-xylanases. The role of cellulase [see 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] and d-xylanase on the overall hydrolysis of pure cellulose and lignocellulosic substrates is discussed.     

Immobilization of Penicillium funiculosum cellulase on a soluble polymer

The three cellulase [see 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] components of Penicillium funiculosum have been immobilized on a soluble, high molecular weight polymer, poly(vinyl alcohol), using carbodiimide. The immobilized enzyme retained over 90% of cellulase [1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4], and exo-β-d-glucanase [1,4-β-d-glucan cellobiohydrolase, EC 3.2.1.91] and β-d-glucosidase [β-d-glucoside glucohydrolase, EC 3.2.1.21] activities. The bound enzyme catalysed the hydrolysis of alkali-treated bagasse with a greater efficiency than the free cellulase. The potential for reuse of the immobilized system was studied using membrane filters and the system was found to be active for three cycles.     

Immobilization of cellulase through its carbohydrate side chains — A rationale for its recovery and reuse

The major types of components of cellulase [see 1,4-(1, 3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] have been adsorbed onto concanavalin A immobilized on Sepharose 4B, suggesting that they are glycoproteins. These components were covalently coupled to cyanogen bromide-activated Sepharose after aminoalkylation of their periodate-oxidized carbohydrate side chains to provide additional points of attachment of the enzyme to the support. Although there was only a 9% recovery of starting avicelase activity, the immobilized enzyme catalysed the hydrolysis of insoluble cellulose to glucose with greater efficiency than did free cellulase.     

Functional characteristics of two d-xylanases purified from Trichoderma harzianum

Two endo-1,4-β-d-xylanases (1,4-β-d-xylan xylanohydrolase, EC 3.2.1.8) were purified from Trichoderma harzianum culture filtrates. From kinetic analyses, apparent V_max and K_m values of 580 U mg^?1 protein and 0.16% d-xylan were obtained for the 20 000 dalton endo-1,4-β-d-xylanase, while values of 100 U mg^?1 protein and 0.066% d-xylan were obtained for the 29 000 dalton endo-1,4-β-d-xylanase. Substrate levels >1% (w/v) d-xylan were found to be inhibitory to both enzymes. Both d-xylanases were highly active against d-xylans obtained from various sources. Of the polymeric sugars tested, carboxymethyl cellulose was the only substrate which was hydrolysed to any extent. Little or no activity was observed against cellulose. Analyses by h.p.l.c. demonstrated the absence of hydrolytic activity by both d-xylanases on d-xylobiose. d-Xylotriose was cleaved to a limited extent by the 29 000 dalton d-xylanase only, while d-xylotetraose was hydrolysed by both. In the presence of d-xylotetraose, the 20 000 dalton d-xylanase had an associated transxylosidase activity which was not observed with the 29 000 dalton enzyme. When the solubilization assay was used, neither of the d-xylanases was inhibited by high concentrations of d-xylose and xylobiose.     

Immobilization of enzymes on crosslinked gelatin particles activated with various forms and complexes of titanium(IV) species

A number of methods of activating the surface of glutaraldehyde crosslinked gelatin beads with titanium(IV) compounds, for subsequent enzyme coupling, have been investigated. Glucoamylase (exo-1,4-α-d-glucosidase, EC 3.2.1.3) was so immobilized using titanium(IV)-urea, -acrylamide, -citric acid and -lactose complexes; however, immobilized enzyme preparations with low activities were obtained (0.36–1.28 U g^?1). Activation with uncomplexed titanium(IV) chloride, however, of both moist and freeze-dried crosslinked gelatin particles resulted in highly active immobilized glucoamylase preparations (1.74–26.6 U g^?1). Dual immobilized enzyme conjugates of glucoamylase and invertase (β-d-fructofuranosidase, EC 3.2.1.26) were also prepared using this method. Invertase was served on the entrapped enzyme while glucoamylase was coupled on the surface of titanium(IV)-activated gelatin pre-entrapped invertase particles. A dual gelatin coupled glucoamylase/gelatin entrapped glucoamylase was prepared (3.8 U g^?1) and ～72.5% of the total combined activity was due to the surface bound enzyme.     

Characterization of microbial endo-β-glucanase immobilized in alginate beads

Endo-β-glucanase (endo-β-1,4-glucano-glucanase EC 3.2.1.4), isolated from Trichoderma reesei, was immobilized in calcium alginate beads, retaining 75% of its original activity. The polyanionic moiety surrounding the immobilized enzyme displaced the pH-activity profile to alkaline regions with respect to that of the free enzyme. The enzyme was inhibited by carboxymethylcellulose, but this inhibition appeared to be decreased by immobilizatíon. The enzyme immobilized in alginate beads showed a K_m value (1.02% w/v) lower than that of the enzyme (1.31%). The apparent V_max of immobilized cellulase preparations (238.3 μmol glucose/ml × h) decreased by a factor of 0.59 with respect to that of the soluble enzyme. The optimum temperature (60°C) of the free and entrapped enzymes remained unaltered. In contrast, the half-life of the endoglucanase immobilized in calciumalginate beads was 4.6 h at 55°C and 5.4 h at 60°C, while that of the free enzyme was 3.0 h at 55°C and 1.2 h at 60°C. A technological application of the immobilized enzymes was tested using wheat straw as a source of fermentable sugars. The hydrolytic degradation of straw, by means of a crude extract of free and immobilized cellulases and β-glucosidase, released a large amount of reducing sugars from wheat straw after 48 h (between 250–720 mg glucose/g straw), carrying out more than a 90% saccharification. A mixture of immobilized β-glucosidase and free cellulases maintained 80% of the activity of the soluble counterparts, and the co-immobilization of both types of enzymes reduced by hydrolytic efficiency to half.     

Cellulase and ethanol production from cellulose by Neurospora crassa

Two strains of Neurospora crassa have been identified which utilize cellulase and produce extracellular cellulase [see 1,4-(1,3; 1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] and β-d-glucosidase [β-d-glucoside glucohydrolase, EC 3.2.1.21]. The activities were detected as early as 48 h in the culture broth. These cultures also fermented d-glucose, d-xylose and cellulosic materials to ethanol as the major product of fermentation. The conversion of cellulose to ethanol was >60%, indicating the potential of using Neurospora for the direct conversion of cellulose to ethanol.     

Optimization of the composition of the nutrient medium for cellulase and protein biosynthesis by thermophilic Aspergillus fumigatus NRC 272

An active strain of Aspergillus spp. has been selected for the production of cellulolytic enzymes and proteins when grown on peracetic acid-treated wheat straw. This strain produced a considerable amount of cellulase [see 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] in the extracellular supernatant and exhibited good overall cellulolytic activity, as measured using filter paper and Avicel as substrates. Also, under the same conditions the strain showed high activities of β-d-glucosidase (β-d-glucoside glucohydrolase, EC 3.2.1.21) and β-d-xylosidase (1,4-β-d-xylan xylohydrolase, EC 3.2.1.37). The maximum enzyme yields (carboxymethylcellulose activity 26.4 units ml^?1, filter paper activity 2.26 units ml^?1 and Avicel activity 16.82 units ml^?1; β-d-glucosidase 9.09 units ml^?1 and β-d-xylosidase 1.92 units ml^?1) were obtained after 96 h incubation at 45°C.     

Russian Article pp. 191–195

Three cellulase components and one xylanase of Trichoderma sp. M-17 have been immobilzed on a soluble high molecular weight polymer (PVA), using carbodiimide. The immobilized enzymes retained about 80% of the cellulase, cellulose 1,4-β-cellobiosidase, β-glucosidase and 60% endo-1,4-β-xylanase activities. The bound enzymes catalyzed the hydrolysis of alkali-treated cornstalks with a higher efficiency than the free cellulase. The potential for reutilization of the immobilized enzymes was studied using membrane filters and the system was found to be active for three cycles.     

Purification and properties of two exo-cellobiohydrolases from a cellulolytic culture of Fusarium lini

Two distinct exo-cellobiohydrolases (1,4-β-d-glucan cellobiohydrolase, EC 3.2.1.91) have been isolated from culture filtrates of Fusarium lini by repeated ammonium sulphate fractionation and isoelectric focusing. The purified enzymes were evaluated for physical properties, kinetics and the mechanism of their action. The results of this work were as follows. (1) A two-step enzyme purification procedure was developed, involving isoelectric focusing and ammonium sulphate fractionation. (2) Yields of pure cellobiohydrolases I and II were 45 and 36 mg l^?1 of culture broth, respectively. (3) Both enzymes were found to be homogeneous, as determined by ultracentrifugation, isoelectric focusing, electrophoresis in polyacrylamide gels containing SDS and chromatography on Sephadex. (4) The molecular weights of the two cellobiohydrolases, as determined by gel filtration and SDS gel electrophoresis, were 50 000–57 000. (5) Both cellobiohydrolases had low viscosity-reducing and reducing sugar activity from carboxymethyl cellulose and high activity with Walseth cellulose and Avicel. (6) The enzymes produced only cellobiose as the end product from filter paper and Avicel, indicating that they are true cellobiohydrolases. (7) Cellobiohydrolase I hydrolysed d-xylan whereas cellobiohydrolase II was inactive towards d-xylan. (8) There was a striking synergism in filter paper activity when cellobiohydrolase was supplemented with endo-1,4-β-d-glucanase [cellulase, 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] and β-d-glucosidase (β-d-glucoside glucohydrolase, EC 3.2.1.21).     

Kinetics of the enzymatic hydrolysis of cellulose: 1. A mathematical model for a batch reactor process

A mathematical model for enzymatic cellulose hydrolysis, based on experimental kinetics of the process catalysed by a cellulase [see 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] preparation from Trichoderma longibrachiatum has been developed. The model takes into account the composition of the cellulase complex, the structural complexity of cellulose, the inhibition by reaction products, the inactivation of enzymes in the course of the enzymatic hydrolysis and describes the kinetics of d-glucose and cellobiose formation from cellulose. The rate of d-glucose formation decelerated through the hydrolysis due to a change in cellulose reactivity and inhibition by the reaction product, d-glucose. The rate of cellobiose formation decelerated due to inhibition by the product, cellobiose, and inactivation of enzymes adsorbed on the cellulose surface. Inactivation of the cellobiose-producing enzymes as a result of their adsorption was found to be reversible. The model satisfactorily predicts the kinetics of d-glucose and cellobiose accumulation in a batch reactor up to 70–80% substrate conversion on changing substrate concentration from 5 to 100 g l^?1and the concentration of the enzymic preparation from 5 to 60 g l^?1.     

Studies on enzymic methods for extraction of inulin from Jerusalem artichokes

The release of inulin, d-fructose and protein from Jerusalem artichokes has been studied under diffusion and maceration conditions. The effects on release of added inulinase (2,1-β-d-fructan fructanohydrolase, EC 3.2.1.7), protease and cellulase [see 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] enzymes have been investigated. The results indicate that added enzymes do not improve the efficiency of inulin or d-fructose release and that mechanical methods represent the most efficient means of carbohydrate solubilization. Treatment of plant extracts with inulinase is shown to have the disadvantage of increasing peptide solubilization. The potential for improved inulin solubilization by use of endo-inulinases is discussed.     

Effect of attached carbohydrates on the activity of Trichoderma viride cellulases

Trichoderma viride 1,4-β-d-glucan cellobiohydrolase (exo-cellobiohydrolase, 1,4-β-d-glucan cellobiohydrolase, EC 3.2.1.91) purified from a commercial product to electrophoretic homogeneity by a procedure including affinity and DEAE-Sephadex chromatography, has attached carbohydrates in addition to the glycoprotein constituents. These carbohydrates are lost by consecutive gel filtration steps in Sephadex G-25 columns, whereupon there is a rapid increase in enzymatic activity. A single gel filtration step can eliminate d-glucose or cellobiose added to a solution of this enzyme, but not the carbohydrates attached during incubation with Avicel.After free carbohydrate elimination from crude cellulase complexes by Sephadex G-25 chromatography, liberation of d-glucose following incubation at 50°C and pH 4.8 was observed. This indicates that some carbohydrates remain bound after gel filtration. The elimination of carbohydrate from whole cellulase complex [see 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] was favoured by a yeast treatment, with a simultaneous increase in activity, but the process is not reproducible, as a secondary inactivation process exists.     

Application of cellulase and pectinase from fungal origin for the liquefaction and saccharification of biomass

Commercial cellulase [see 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] from Trichoderma viride and pectinase [poly(1,4-α-d-galacturonide) glycanohydrolase, EC 3.2.1.15] from Aspergillus niger have been applied to produce fermentation syrups from sugar-beet pulp and potato fibre. Cellulosic, hemicellulosic and pectic polysaccharides of these substrates were hydrolysed extensively. Recovery of enzymes has been investigated in a packed-column reactor, connected with a hollow-fibre ultrafiltration unit. Enzymes appeared to be stable in this type of reactor, although part of the enzyme activity was lost, especially by adsorption onto the substrate residue.     

Kinetics of the enzymatic hydrolysis of cellulose: 2. A mathematical model for the process in a plug-flow column reactor

The kinetics of enzymatic cellulose hydrolysis in a plug-flow column reactor catalysed by cellulases [see 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] from Trichoderma longibrachiatum adsorbed on cellulose surface have been studied. The maximum substrate conversion achieved was 90–94%. The possibility of enzyme recovery for a reactor of this type is discussed. A mathematical model for enzymatic cellulose hydrolysis in a plug-flow column reactor has been developed. The model allows for the component composition of the cellulase complex, adsorption of cellulases on the substrate surface, inhibition by reaction products, changes in cellulose reactivity and the inactivation of enzymes in the course of hydrolysis. The model affords a reliable prediction of the kinetics of d-glucose and cellobiose formation from cellulose in a column reactor as well as the degree of substrate conversion and reactor productivity with various amounts of adsorbed enzymes and at various flow rates.     

Purification and characterization of two d-xylanases from Trichoderma harzianum

Two endo-1,4-β-d-xylanases (1,4-β-d-xylan xylanohydrolase, EC 3.2.1.8) from Trichoderma harzianum E58 have been purified by ultrafiltration and chromatography on carboxymethyl-Sepharose, phenyl-Sepharose and Sephadex G-75. The d-xylanases were shown to be homogeneous by the criteria of dodecyl sulphate polyacrylamide gel electrophoresis and isoelectric focusing. The molecular weights were estimated to be 20 000 and 29 000, with pl values of 9.4 and 9.5, respectively. Typically, 456 mg of the 20 000 dalton and 1.9 mg of the 29 000 dalton d-xylanases were purified from 4.2 litre of culture filtrate with specific activities of 370 and 75 U mg^?1, respectively. Optimum d-xylanase activities were obtained when the enzymes were incubated at pH 5, 50°C, for the 20 000 dalton protein and pH 5, 60°C for the 29 000 dalton protein.     

Isolation of mutants of Talaromyces emersonii CBS 814.70 with enhanced cellulase activity

By a combination of genetic mutation and modification of growth medium the cellulase [see 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4 etc.] activity of culture filtrates of Talaromyces emersonii CBS 814.70 has been increased four-fold to approximately 2 U ml^?1 and a productivity of 20–25 Ul^?1h^?1. At 50°C this system was completely stable for at least 24 h. At 60°C in static reaction mixtures 19% of the original activity was lost compared with 21% when mixtures were shaken. At 70°C the loss of activity after 4 h was 64% without shaking and 70% when shaken. The cellulase system from Trichoderma reesei was decidedly less stable than that of Talaromyces emersonii under each of the above conditions. The ability of each enzyme system, separately and together, to digest beet pulp was investigated.     

Mutants of the white-rot fungus Sporotrichum pulverulentum with increased cellulase and β-d-glucosidase production

This paper reports the isolation of mutants of the white-rot fungus Sporotrichum pulverulentum and the results of a survey of enzymic activity among these mutants. The strains were screened for extracellular cellulase [see 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] and β-d-glucosidase (β-d-glucoside glucohydrolase, EC 3.2.1.21) production in shake flask experiments. Apart from strain 63-2, strains 6, 63, 9, L5, E-1 and UV-18 showed equal or higher endo-1,4-β-d-glucanase (cellulase), filter paper-degrading and β-d-glucosidase activities than S. pulverulentum. The cellulase activity obtained, measured as filter paper activity, was comparable to that reported for Trichoderma reesei QM9414. However, the β-d-glucosidase activity was about six times higher than for the QM9414 strain. The pH and temperature-activity profiles of crude β-d-glucosidase preparations from the various strains were determined and were found to be identical. The thermal stability at pH 4.5 and 40°C was 5 days for all these preparations.     

Enhanced cellulase production in fed-batch culture of Trichoderma reesei C30

The use of a fed-batch cultivation of the fungus Trichoderma reesei (C30) allows cellulase [see 1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] production to occur under optimum conditions, and results in extremely high enzyme titres and productivities. Enzyme levels of 26 U ml^?1 at productivities >130 U l^?1 h^?1 have been achieved. These results are compared with the values obtained in two-stage continuous cultivation of the organism at optimum pH and temperature.