Construction of Highly efficient cellulase compositions for enzymatic hydrolysis of cellulose

Abstract

This invention provides novel enzyme compositions using newly identified and isolated C. lucknowense enzymes, including CBH Ib CBH IIb, EG II, EG VI, β-glucosidase, and xylanase II in conjunction with previously identified enzymes CBH Ia, CBH IIa (previously described as Endo 43), and EG V. These enzyme compositions demonstrate an extremely high ability to convert lignocellulosic biomass (e.g., Avicel, cotton, Douglas fir wood pretreated by organosolv) to glucose. CBH Ia and IIb, which both have a cellulose-binding module (CBM) displayed a pronounced synergism with three major endoglucanases (EG II, EG V, EG VI) from the same fungus in hydrolysis of cotton as well as a strong synergy with each other. The enzyme compositions are effective in hydrolysis of the lignocellulosic biomass.

Description

FIELD OF THE INVENTION

This invention relates to compositions and methods for producing bioenergy or other value-added products from lignocellulosic biomass or cellulosic materials. In particular, the invention provides enzyme compositions capable of converting a variety of cellulosic substrates or lignocellulosic biomass into a fermentable sugar. The invention also provides methods for using such enzyme compositions.

INTRODUCTION

Bioconversion of renewable lignocellulosic biomass to a fermentable sugar that is subsequently fermented to produce alcohol (e.g., ethanol) as an alternative to liquid fuels has attracted an intensive attention of researchers since 1970s, when the oil crisis broke out because of decreasing the output of petroleum by OPEC (Bungay H. R., “Energy: the biomass options”. NY: Wiley; 1981; Olsson L, Hahn-Hägerdal B. “Fermentation of lignocellulosic hydrolysates for ethanol production”, Enzyme Microb Technol 1996; 18:312-31; Zaldivar J, Nielsen J, Olsson L. “Fuel ethanol production from lignocellulose: a challenge for metabolic engineering and process integration”, Appl Microbiol Biotechnol 2001; 56:17-34; Galbe M, Zacchi G., “A review of the production of ethanol from softwood”, Appl Microbiol Biotechnol 2002; 59:618-28). Ethanol has been widely used as a 10% blend to gasoline in the USA or as a neat fuel for vehicles in Brazil in the last two decades. The importance of fuel bioethanol will increase in parallel with skyrocketing prices for oil and gradual depletion of its sources. Additionally, fermentable sugars are being used to produce plastics, polymers and other biobased products and this industry is expected to grow substantially therefore increasing the demand for abundant low cost fermentable sugars which can be used as a feed stock in lieu of petroleum based feedstocks (e.g. see article “The Rise Of Industrial Biotech” published in Forbes Jul. 24, 2006)

The major polysaccharides comprising different lignocellulosic residues, which may be considered as a potential renewable feedstock, are cellulose and hemicelluloses (xylans). The enzymatic hydrolysis of these polysaccharides to soluble sugars, for example glucose, xylose, arabinose, galactose, mannose, and other hexoses and pentoses occurs under the action of different enzymes acting in concert. Endo-1,4-β-glucanases (EG) and exo-cellobiohydrolases (CBH) catalyze the hydrolysis of insoluble cellulose to cellooligosaccharides (cellobiose as a main product), while β-glucosidases (BGL) convert the oligosaccharides to glucose. Xylanases together with other accessory enzymes (non-limiting examples of which include α-L-arabinofuranosidases, feruloyl and acetylxylan esterases, glucuronidases, and β-xylosidases) catalyze the hydrolysis of hemicelluloses.

Regardless of the type of cellulosic feedstock, the cost and hydrolytic efficiency of enzymes are major factors that restrict the commercialization of the biomass bioconversion processes. The production costs of microbially produced enzymes are tightly connected with a productivity of the enzyme-producing strain and the final activity yield in the fermentation broth. The hydrolytic efficiency of a multienzyme complex in the process of lignocellulose saccharification depends both on properties of individual enzymes, the synergies between them, and their ratio in the multienzyme cocktail.

Chrysosporium lucknowense is a fungus that is known to produce a wide variety of cellulases, hemicellulases, and possibly other accessory enzymes. C. lucknowense also secrets at least five different endoglucanases, the EG II (51 kDa, Ce15A) being the most active. Moreover, C. lucknowense mutant strains (including UV18-25) have been developed to produce enzymes for textile, pulp and paper, detergent and other applications, but not for the enzymatic saccharification of cellulose; these strains can also be used for a high-level production of homologous and heterologous proteins. The best C. lucknowense mutant strains secrete at least 50-80 gl⁻¹ of extracellular protein in low viscosity fermentations. The full fungal genome of the C. lucknowense has been sequenced in 2005 (see http://www.dyadic-group.com/wt/dyad/pr_—1115654417), and now the genome annotation is being carried out.

The crude C. lucknowense multienzyme complex demonstrates modest results in cellulose saccharification, with only a fraction of the cellulose being converted to glucose under the conditions tested. Two cellobiohydrolases of C. lucknowense, belonging to families 7 and 6 of glycoside hydrolases: CBH Ia (Ce17A) and CBH IIa (Ce16A), have been previously isolated and studied. CBH Ia was previously referred to as CBH I, 70(60) kD protein in U.S. Pat. No. 6,573,086. CBH Ia exists in the culture broth as a full size enzyme (observed molecular mass 65 kDa, SDS-PAGE data), consisting of a core catalytic domain and cellulose-binding module (CBM) connected by a flexible peptide linker, and its truncated form (52 kDa), representing the enzyme catalytic domain. CBH I (Ce17A) of C. lucknowense appears to be slightly less effective in hydrolysis of crystalline cellulose but more thermostable than the CBH I of T. reesei. CBH IIa was previously thought to be an endoglucanase and has been referred to as 43 kD Endo and EG6. See, e.g., U.S. Pat. No. 6,573,086. CBH IIa (43 kDa) has no CBM, i.e. its molecule contains only the catalytic domain.

In spite of the continued research of the last few decades to understand enzymatic lignocellulosic biomass degradation and cellulase production, it remains desirable to discover or to engineer new highly active cellulases and hemicellulases. It would also be highly desirable to construct highly efficient enzyme compositions capable of performing rapid and efficient biodegradation of lignocellulosic materials.

SUMMARY OF THE INVENTION

This invention provides several newly identified and isolated enzymes from C. lucknowense. The new enzymes include two new cellobiohydrolases (CBH Ib and IIb, or Ce17B and Ce16B), an endoglucanase (EG VI), (not to be confused with CBH IIa, which was previously referred to as EG 6)a β-glucosidase (BGL), and a xylanase (Xyl II). The CBH IIb has a high activity against Avicel and cotton and displayed a pronounced synergism with other C. lucknowense cellulases. Using these new enzymes, this invention provides highly effective enzyme compositions for cellulose hydrolysis.

One object of this invention is to provide an enzyme formulation that includes at least one isolated cellobiohydrolase obtained from C. lucknowense. The isolated cellobiohydrolase may be either CBH Ib and IIb. The enzyme formulation may optionally contain an endoglucanase and/or a β-glucosidase. Furthermore, the enzyme formulation may optionally contain a hemicellulase.

Another object of this invention is to provide a method for producing glucose from cellulose. The method includes producing an enzyme formulation that contains at least one isolated cellobiohydrolase obtained from C. lucknowense, which can be CBH Ib or IIb. Optionally, the enzyme formulation may contain an endoglucanase and/or a β-glucosidase. The enzyme formulation is applied to cellulose to form glucose.

Yet another aspect of this invention is to provide a method of producing ethanol. The method includes providing an enzyme formulation that contains at least one isolated cellobiohydrolase obtained from C. lucknowense, which can be CBH Ib or IIb. The enzyme formulation optionally may contain an endoglucanase and/or a β-glucosidase. Furthermore, the enzyme formulation may optionally contain a hemicellulase. The method further includes applying the enzyme formulation to cellulose to produce glucose and subsequently fermenting the glucose to produce ethanol.

This invention also provides a method of producing energy from ethanol. The method includes providing an enzyme formulation that contains at least one isolated cellobiohydrolase obtained from C. lucknowense, which can be CBH Ib or IIb. The enzyme formulation optionally may contain an endoglucanase and/or a β-glucosidase. Furthermore, the enzyme formulation may optionally contain a hemicellulase. The method further includes applying the enzyme formulation to cellulose to produce glucose, fermenting the glucose to produce ethanol, and combusting said ethanol to produce energy.

Another aspect of this invention is to provide a mutant Chrysosporium lucknowense strain capable of expressing at least one cellobiohydrolase and at least one endo-1,4-β-glucanase at higher levels than the corresponding non-mutant strain under the same conditions. The cellobiohydrolase is selected from the group consisting of CBH Ia, CBH IIa, CBH Ib, and CBH IIb; and the endo-1,4-β-glucanase is selected from the group consisting of EG II, EG V, and EG VI.

Yet another aspect of this invention is to provide proteins exhibiting at least 65% amino acid identity as determined by the BLAST algorithm with the CBH Ib, CBH IIb, EG VI, BGL, and Xyl II amino acid sequences of SEQ ID NOs. 2, 4, 16, 12, and 18, respectively, or a part thereof having at least 20 contiguous amino acids. This invention also contemplates the corresponding nucleic acid sequences that encode such a protein.

One aspect of this invention provides an enzyme formulation comprising at least one enzyme selected from the group consisting of CBH Ib, CBH IIb, EG II, EG VI, BGL, and Xyl II.

Another aspect of this invention provides a method of producing fermentable sugars from lignocellulosic material. The method comprises (a) providing an enzyme formulation comprising at least one enzyme selected from the group consisting of CBH Ib, CBH IIb, EG II, EG VI, BGL, and Xyl II; and (b) applying the enzyme formulation to lignocellulosic material to produce fermentable sugars.

The invention also provides a method of producing a fermentation product or a starting material for a fermentation product from a fermentable sugar. This method comprises comprises (a) providing an enzyme formulation, wherein the enzyme formulation contains at least one enzyme selected from the group consisting of CBH Ib, CBH IIb, EG II, EG VI, BGL, and Xyl II; (b) applying the enzyme formulation to lignocellulosic material to produce a fermentable sugar; and (c) fermenting said fermentable sugar to produce a fermentation product.

In another aspect, the invention provides a method of producing energy from a fermentable sugar. The method comprises (a) providing an enzyme formulation, wherein the enzyme formulation comprises at least one enzyme selected from the group consisting of CBH Ib, CBH IIb, EG II, EG VI, BGL, and Xyl II; (b) applying the enzyme formulation to lignocellulosic material to produce a fermentable sugar; (c) fermenting the fermentable sugar to produce a combustible fermentation product; and (d) combusting said combustible fermentation product to produce energy.

One object of the invention is provide a mutant Chrysosporium lucknowense strain capable of expressing at least one cellobiohydrolase and at least one endo-1,4-β-glucanase at higher levels than the corresponding non-mutant strain under the same conditions. The cellobiohydrolase is selected from the group consisting of CBH Ia, CBH Ib, CBH IIa and CBH IIb; and the endo-1,4-β-glucanase is selected from the group consisting of EG II, EG V, and EG VI.

The invention also provides a protein exhibiting at least 65% amino acid identity as determined by the BLAST algorithm with the CBH Ib, IIb, EG VI, BGL, Xyl II amino acid sequences as defined herein or a part thereof having at least 20 contiguous amino acids.

Another aspect of this invention provides a nucleic acid sequence having at least 80% homology with the nucleic acid sequence encoding CBH Ib, CBH IIb, EG II, EG VI, BGL, or Xyl II, as defined herein.

The invention also provides a method for degrading a lignocellulosic material to fermentable sugars. The method includes contacting the lignocellulosic material with an effective amount of a multi-enzyme product derived from a microorganism, to produce at least one fermentable sugar. At least one enzyme in the multi-enzyme product is selected from the group consisting of CBH Ia, CBH Ib, CBH IIa, CBH IIb, EG II, EG V, EG VI, BGL, and Xyl II.

In another aspect, the invention provides a microorganism or plant capable of expressing one or more of an enzyme selected from the group consisting of CBH Ia, CBH Ib, CBH IIa, CBH IIb, EG II, EG V, EG VI, BGL, and Xyl II.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1: SDS/PAGE (A) and isoelectrofocusing (B) of purified cellobiohydrolases from C. lucknowense. Lanes: 1, markers with different molecular masses; 2 and 5, CBH Ib; 3 and 6, CBH IIb; 4, markers with different pI.

FIG. 2: Progress kinetics of Avicel (5 mg ml⁻¹) hydrolysis by purified cellobiohydrolases (0.1 mg ml⁻¹) in the presence of purified A. japonicus BGL (0.5 U ml⁻¹), 40° C., pH 5.0.

FIG. 3: Synergism between CBH IIb and other C. lucknowense purified enzymes during hydrolysis of cotton cellulose (5 mg ml⁻¹) in the presence of purified A. japonicus BGL (0.5 U ml⁻¹), 40° C., pH 5.0. The CBH and EG concentration was 0.15 and 0.05 mg ml⁻¹, respectively. Experimental data for the pairs of enzymes are shown with open symbols (continuous curves); the theoretical sums of glucose concentrations obtained under the action of individual enzymes are shown with filled symbols (dotted lines).

FIG. 4: Progress kinetics of cotton (25 mg ml⁻¹) hydrolysis by combination #1 of purified C. lucknowense enzymes and NCE L-600, a commercial C. lucknowense multienzyme cellulase preparation at protein loading of 0.5 mg ml⁻¹, 50° C., pH 5.0 (see text and Table 4 for details).

FIG. 5: Progress kinetics of Avicel (50 mg ml⁻¹) hydrolysis by combination #1 of purified C. lucknowense enzymes and NCE-L, a commercial C. lucknowense multienzyme cellulase preparation at protein loading of 0.5 mg ml⁻¹, 50° C., pH 5.0 (see text and Table 4 for details).

FIG. 6: Progress kinetics of hydrolysis of pretreated Douglas fir wood (50 mg ml⁻¹) by combination #1 of purified C. lucknowense enzymes and NCE-L 600, a commercial C. lucknowense at protein loading of 0.5 mg ml⁻¹, 50° C., pH 5.0 (see text and Table 4 for details).

FIG. 7: Progress kinetics of hydrolysis of pretreated Douglas fir wood (50 mg ml⁻¹) by different combinations of purified C. lucknowense enzymes at protein loading of 0.5 mg ml⁻¹, 50° C., pH 5.0 (see text and Table 5 for details).

FIG. 8: cbh2 gene encoding CBH IB.

FIG. 9: cbh4 gene encoding CBH IIb

FIG. 10: cbh1 gene encoding CBH Ia

FIG. 11: EG6 gene encoding CBH IIa

FIG. 12: eg2 gene encoding EG II

FIG. 13: bgl1 gene encoding BGL

FIG. 14; eg5 gene encoding EGV

FIG. 15: eg7 gene encoding EGVI

FIG. 16: xyl2 gene encoding Xyl II

DETAILED DESCRIPTION OF THE INVENTION

The present invention provides methods and compositions for the conversion of plant biomass to fermentable sugars that can be converted to useful products. The methods include methods for degrading lignocellulosic material using enzyme mixtures to liberate sugars. The compositions of the invention include enzyme combinations that break down lignocellulose. As used herein the terms “biomass” or lignocellulosic material” includes materials containing cellulose and/or hemicellulose. Generally, these materials also contain xylan, lignin, protein, and carbohydrates, such as starch and sugar. Lignocellulose is generally found, for example, in the stems, leaves, hulls, husks, and cobs of plants or leaves, branches, and wood of trees. The process of converting a complex carbohydrate (such as starch, cellulose, or hemicellulose) into fermentable sugars is also referred to herein as “saccharification.” Fermentable sugars, as used herein, refers to simple sugars, such as glucose, xylose, arabinose, galactose, mannose, rhamnose, sucrose and fructose.

Biomass can include virgin biomass and/or non-virgin biomass such as agricultural biomass, commercial organics, construction and demolition debris, municipal solid waste, waste paper and yard waste. Common forms of biomass include trees, shrubs and grasses, wheat, wheat straw, sugar cane bagasse, corn, corn husks, corn kernel including fiber from kernels, products and by-products from milling of grains such as corn, wheat and barley (including wet milling and dry milling) as well as municipal solid waste, waste paper and yard waste. The biomass can also be, but is not limited to, herbaceous material, agricultural residues, forestry residues, municipal solid wastes, waste paper, and pulp and paper mill residues. “Agricultural biomass” includes branches, bushes, canes, corn and corn husks, energy crops, forests, fruits, flowers, grains, grasses, herbaceous crops, leaves, bark, needles, logs, roots, saplings, short rotation woody crops, shrubs, switch grasses, trees, vegetables, fruit peels, vines, sugar beet pulp, wheat midlings, oat hulls, and hard and soft woods (not including woods with deleterious materials). In addition, agricultural biomass includes organic waste materials generated from agricultural processes including farming and forestry activities, specifically including forestry wood waste. Agricultural biomass may be any of the aforestated singularly or in any combination or mixture thereof.

The fermentable sugars can be converted to useful value-added fermentation products, non-limiting examples of which include amino acids, vitamins, pharmaceuticals, animal feed supplements, specialty chemicals, chemical feedstocks, plastics, solvents, fuels, or other organic polymers, lactic acid, and ethanol, including fuel ethanol. Specific value-added products that may be produced by the methods of the invention include, but not limited to, biofuels (including ethanol and butanol); lactic acid; plastics; specialty chemicals; organic acids, including citric acid, succinic acid and maleic acid; solvents; animal feed supplements; pharmaceuticals; vitamins; amino acids, such as lysine, methionine, tryptophan, threonine, and aspartic acid; industrial enzymes, such as proteases, cellulases, amylases, glucanases, lactases, lipases, lyases, oxidoreductases, transferases and xylanases; and chemical feedstocks.

As used herein, a multi-enzyme product can be obtained from or derived from a microbial, plant, or other source or combination thereof, and will contain enzymes capable of degrading lignocellulosic material. Examples of enzymes comprising the multi-enzyme products of the invention include cellulases (such as cellobiohydrolases, endoglucanase, β-glucosidases, hemicellulases (such as xylanases, including endoxylanases, exoxylanase, and β-xylosidase), ligninases, amylases, α-arabinofuranosidases, α-glucuronidases, α-glucuronidases, arabinases, glucuronidases, proteases, esterases (including ferulic acid esterase and acetylxylan esterase), lipases, glucomannanases, and xylogluconases.

In some embodiments, the multi-enzyme product comprises a hemicellulase. Hemicellulose is a complex polymer, and its composition often varies widely from organism to organism, and from one tissue type to another. In general, a main component of hemicellulose is beta-1,4-linked xylose, a five carbon sugar. However, this xylose is often branched as beta-1,3 linkages, and can be substituted with linkages to arabinose, galactose, mannose, glucuronic acid, or by esterification to acetic acid. Hemicellulose can also contain glucan, which is a general term for beta-linked six carbon sugars. Those hemicelluloses include xyloglucan, glucomannan, and galactomannan.

The composition, nature of substitution, and degree of branching of hemicellulose is very different in dicotyledonous plants (dicots, i.e., plant whose seeds have two cotyledons or seed leaves such as lima beans, peanuts, almonds, peas, kidney beans) as compared to monocotyledonous plants (monocots; i.e., plants having a single cotyledon or seed leaf such as corn, wheat, rice, grasses, barley). In dicots, hemicellulose is comprised mainly of xyloglucans that are 1,4-beta-linked glucose chains with 1,6-beta-linked xylosyl side chains. In monocots, including most grain crops, the principal components of hemicellulose are heteroxylans. These are primarily comprised of 1,4-beta-linked xylose backbone polymers with 1,3-beta linkages to arabinose, galactose and mannose as well as xylose modified by ester-linked acetic acids. Also present are branched beta glucans comprised of 1,3- and 1,4-beta-linked glucosyl chains. In monocots, cellulose, heteroxylans and beta glucans are present in roughly equal amounts, each comprising about 15-25% of the dry matter of cell walls.

Hemicellulolytic enzymes, i.e. hemicellulases, include includes both exohydrolytic and endohydrolytic enzymes, such as xylanase, β-xylosidase and esterases, which actively cleave hemicellulosic material through hydrolysis. These xylanase and esterase enzymes cleave the xylan and acetyl side chains of xylan and the remaining xylo-oligomers are unsubstituted and can thus be hydrolysed with Pxylosidase only. In addition, several less known side activities have been found in enzyme preparations which hydrolyse hemicellulose. While the multi-enzyme product may contain many types of enzymes, mixtures comprising enzymes that increase or enhance sugar release from biomass are preferred, including hemicellulases. In one embodiment, the hemicullulase is a xylanase, an arabinofuranosidase, an acetyl xylan esterase, a glucuronidase, an endo-galactanase, a mannanase, an endo arabinase, an exo arabinase, an exo-galactanase, a ferulic acid esterase, a galactomannanase, a xylogluconase, or mixtures of any of these. In particular, the enzymes can include glucoamylase, β-xylosidase and/or β-glucosidase. The enzymes of the multi-enzyme product can be provided by a variety of sources. In one embodiment, the enzymes can be produced by growing microorganisms or plants which produce the enzymes naturally or by virtue of being genetically modified to express the enzyme or enzymes. In another embodiment, at least one enzyme of the multi-enzyme product is commercially available.

One embodiment of the present invention relates to an isolated enzyme for catalyzing the conversion of lignocellulosic material to fermentable sugars as described herein, a homologue thereof, and/or a fragment thereof. Also included in the invention are isolated nucleic acid molecules encoding any of such proteins, homologues or fragments thereof. According to the present invention, an isolated protein or polypeptide is a protein that has been removed from its natural milieu (i.e., that has been subject to human manipulation) and can include purified proteins, partially purified proteins, recombinantly produced proteins, and synthetically produced proteins, for example. As such, “isolated” does not reflect the extent to which the protein has been purified. Preferably, an isolated protein of the present invention is produced recombinantly. An isolated peptide can be produced synthetically (e.g., chemically, such as by peptide synthesis) or recombinantly. An isolated protein can also be provided as a crude fermentation product, or a protein preparation that has been partially purified or purified (e.g., from a microorganism) using protein purification procedures known in the art. In addition, and solely by way of example, a protein referenced as being derived from or from a particular organism, such as a “Chrysosporium lucknowense cellulase and/or hemicellulase” refers to a cellulase and/or hemicellulase (generally including a homologue of a naturally occurring cellulose and/or hemicellulase) from a Chrysosporium lucknowense microorganism, or to a cellulase and/or hemicellulase that has been otherwise produced from the knowledge of the structure (e.g., sequence), and perhaps the function, of a naturally occurring cellulase and/or hemicellulase from Chrysosporium lucknowense. In other words, general reference to a Chrysosporium lucknowense cellulase and/or hemicellulase or a cellulase and/or hemicellulase derived from Chrysosporium lucknowense includes any cellulase and/or hemicellulase that has substantially similar structure and function of a naturally occurring cellulase and/or hemicellulase from Chrysosporium lucknowense or that is a biologically active (i.e., has biological activity) homologue of a naturally occurring cellulase and/or hemicellulase from Chrysosporium lucknowense as described in detail herein. As such, a Chrysosporium lucknowense cellulase and/or hemicellulase can include purified, partially purified, recombinant, mutated/modified and synthetic proteins. The same description applies to reference to other proteins or peptides described herein and to other microbial sources for such proteins or peptides.

One embodiment of the present invention relates to isolated nucleic acid molecules comprising, consisting essentially of, or consisting of nucleic acid sequences that encode any of the enzymes described herein, including a homologue or fragment of any of such enzymes, as well as nucleic acid sequences that are fully complementary thereto. In accordance with the present invention, an isolated nucleic acid molecule is a nucleic acid molecule that has been removed from its natural milieu (i.e., that has been subject to human manipulation), its natural milieu being the genome or chromosome in which the nucleic acid molecule is found in nature. As such, “isolated” does not necessarily reflect the extent to which the nucleic acid molecule has been purified, but indicates that the molecule does not include an entire genome or an entire chromosome in which the nucleic acid molecule is found in nature. An isolated nucleic acid molecule can include a gene. An isolated nucleic acid molecule that includes a gene is not a fragment of a chromosome that includes such gene, but rather includes the coding region and regulatory regions associated with the gene, but no additional genes that are naturally found on the same chromosome. An isolated nucleic acid molecule can also include a specified nucleic acid sequence flanked by (i.e., at the 5′ and/or the 3′ end of the sequence) additional nucleic acids that do not normally flank the specified nucleic acid sequence in nature (i.e., heterologous sequences). Isolated nucleic acid molecule can include DNA, RNA (e.g., mRNA), or derivatives of either DNA or RNA (e.g., cDNA). Preferably, an isolated nucleic acid molecule of the present invention is produced using recombinant DNA technology (e.g., polymerase chain reaction (PCR) amplification, cloning) or chemical synthesis. A nucleic acid molecule homologue can be produced using a number of methods known to those skilled in the art (see, for example, Sambrook et al., Molecular Cloning: A Laboratory Manual, Cold Spring Harbor Labs Press (1989)). For example, nucleic acid molecules can be modified using a variety of techniques including, but not limited to, classic mutagenesis techniques and recombinant DNA techniques, such as site-directed mutagenesis, chemical treatment of a nucleic acid molecule to induce mutations, restriction enzyme cleavage of a nucleic acid fragment, ligation of nucleic acid fragments, PCR amplification and/or mutagenesis of selected regions of a nucleic acid sequence, synthesis of oligonucleotide mixtures and ligation of mixture groups to “build” a mixture of nucleic acid molecules and combinations thereof. Nucleic acid molecule homologues can be selected from a mixture of modified nucleic acids by screening for the function of the protein encoded by the nucleic acid and/or by hybridization with a wild-type gene.

Another embodiment of the present invention includes a recombinant nucleic acid molecule comprising a recombinant vector and a nucleic acid sequence encoding protein or peptide having at least one enzymatic activity useful for catalyzing the conversion of lignocellulosic material to fermentable sugars. According to the present invention, a recombinant vector is an engineered (i.e., artificially produced) nucleic acid molecule that is used as a tool for manipulating a nucleic acid sequence of choice and for introducing such a nucleic acid sequence into a host cell. The recombinant vector is therefore suitable for use in cloning, sequencing, and/or otherwise manipulating the nucleic acid sequence of choice, such as by expressing and/or delivering the nucleic acid sequence of choice into a host cell to form a recombinant cell. Such a vector typically contains heterologous nucleic acid sequences, that is nucleic acid sequences that are not naturally found adjacent to nucleic acid sequence to be cloned or delivered, although the vector can also contain regulatory nucleic acid sequences (e.g., promoters, untranslated regions) which are naturally found adjacent to nucleic acid molecules of the present invention or which are useful for expression of the nucleic acid molecules of the present invention (discussed in detail below). The vector can be either RNA or DNA, either prokaryotic or eukaryotic, and typically is a plasmid. The vector can be maintained as an extrachromosomal element (e.g., a plasmid) or it can be integrated into the chromosome of a recombinant organism (e.g., a microbe or a plant). The entire vector can remain in place within a host cell, or under certain conditions, the plasmid DNA can be deleted, leaving behind the nucleic acid molecule of the present invention. The integrated nucleic acid molecule can be under chromosomal promoter control, under native or plasmid promoter control, or under a combination of several promoter controls. Single or multiple copies of the nucleic acid molecule can be integrated into the chromosome. A recombinant vector of the present invention can contain at least one selectable marker.

Typically, a recombinant nucleic acid molecule includes at least one nucleic acid molecule of the present invention operatively linked to one or more expression control sequences. According to the present invention, the phrase “operatively linked” refers to linking a nucleic acid molecule to an expression control sequence (e.g., a transcription control sequence and/or a translation control sequence) in a manner such that the molecule can be expressed when transfected (i.e., transformed, transduced, transfected, conjugated or conduced) into a host cell. Transcription control sequences are sequences that control the initiation, elongation, or termination of transcription. Particularly important transcription control sequences are those that control transcription initiation, such as promoter, enhancer, operator and repressor sequences.

Suitable transcription control sequences include any transcription control sequence that can function in a host cell or organism into which the recombinant nucleic acid molecule is to be introduced.

Enzymes and Nucleic Acids Encoding the Enzymes

As described in the examples, this invention provides several purified enzymes, including two cellobiohydrolases, (CBH Ib, SEQ ID NO. 2; CBH IIb, SEQ ID NO. 4), an endoglucanase (EG VI, SEQ ID NO. 16), a β-glucosidase (BGL, SEQ ID NO. 12), and a xylanase (Xyl II, SEQ ID NO. 18). This invention also contemplates variants of such enzymes, including variants having amino acid sequence with at least 65%, 70%, or 75% amino acid identity with these enzymes, as determined by the conventionally used BLAST algorithm.

Additionally, the invention provides the nucleic acids that encode these sequences, including gene cbh2 (SEQ ID NO. 1, encoding CBH Ib), gene cbh4 (SEQ ID NO. 3, encoding CBH IIb); gene eg7 (SEQ ID NO. 15, encoding EG VI), gene bgl1 (SEQ ID NO. 11, encoding BGL), and gene xyl2 (SEQ ID NO. 17, encoding Xyl II). This invention also contemplates variants of these nucleic acids, including variants that have at least 80%, 85% or 90% homology with these nucleic acids.

As described herein, the newly identified and isolated enzymes according to the invention can be used in conjunction with at least one other enzyme that promotes saccharification of cellulosic materials. In preferred embodiments, this additional enzyme is derived from C. lucknowense. For example, the enzyme may be CBH Ia (SEQ ID NO. 6), CBH IIa (SEQ ID NO. 8), EG II (SEQ ID NO. 10) or EG V (SEQ ID NO. 14). Note however, that in certain preferred embodiments, CBH Ia, CBH IIa EG II, and EG V may be obtained by genetically modifying a microorganism or plant to express cbh1 (SEQ ID NO. 5, encoding CBH Ia), EG6 (SEQ ID NO. 7, encoding CBH IIa), eg2 (SEQ ID NO. 9, encoding EG II), and/or EG5 (SEQ ID NO. 13, encoding EG V). One particularly useful combination for saccharification is CBH Ia, CBH Ib, CBH IIb, EG II, EG V, BGL, and Xyl II.

In certain embodiments, the polynucleotides and polypeptides of the invention are evolved using molecular evolution techniques to create and to identify novel variants with desired structural, functional, and/or physical characteristics. Molecular evolution techniques can be “DNA Shuffling”, or “sexual PCR” (WPC, Stemmer, PNAS, 91:10747, (1994)), also referred to as “directed molecular evolution”, “exon-shuffling”, “directed enzyme evolution”, “in vitro evolution” and “artificial evolution”. Such reference terms are known in the art and are encompassed by the invention. Characteristics such as activity, the protein's enzyme kinetics, the protein's K_i, K_cat, K_m, V_max, K_d, thermostability, pH optimum, and the like can be modified. In certain embodiments, the polynucleotides and/or polypeptides of the invention may be evolved to confer properties that are advantageous for in situ enzymatic saccharification and fermentation. For example, enzymes may be evolved to perform optimally in an environment which is suitable for fermentation of sugars. In one example, the enzymes are evolved to have maximum activity in an environment with elevated temperature and high ambient alcohol content, such as an environment where an organism such as yeast is fermenting sugars. In this way, saccharification of lignocellulose and fermentation occurs in a single process step. In another example, the enzymes are evolved to resist harsh chemical or thermal environments, such as those that may be experienced during lignocellulosic pretreatments, as described herein. In these embodiments, it is not necessary to chemically or thermally pretreat the lignocellulose prior to adding enzymes. Rather, the treatment and enzymatic saccharification can be performed simultaneously. Of course, this invention also contemplates processes involving multiple steps to produce sugars from lignocellulose, such as those where evolved enzymes first saccharify lignocellulose, which is subsequently fermented by an organism, such as yeast, for example.

In other embodiments, the ability to enhance specific characteristics of a protein may also be applicable to changing the characterized activity of an enzyme to an activity completely unrelated to its initially characterized activity. Other desirable enhancements of the invention would be specific to each individual protein, and would thus be well known in the art and contemplated by the invention.

Expression of Enzymes

The microorganisms useful in the present invention and/or as a source of enzymes useful in the present invention include any microorganism producing an enzyme capable of degrading lignocellulosic material, including bacteria, yeast, and filamentous fungi. For simplicity and convenience, filamentous fungal microorganisms will be discussed herein; however, one skilled in the art will recognize that other microorganisms will be useful in the present invention. Filamentous fungi have been widely used in industry for the production of proteins. These fungi are uniquely adapted for the production and secretion of proteins owing to their biological niche as microbial scavengers. In environments rich in biological polymers, such as forest floors, the fungi compete by secreting enzymes that degrade those polymers, producing monomers that can be readily utilized as nutrients for growth. The natural ability of fungi to produce proteins has been widely exploited, mainly for the production of industrial enzymes. Levels of protein production in natural isolates can be increased in improved strains by orders-of-magnitude; production yields of tens of grams of protein per liter of fermentation culture are commonplace.

Fungal strains, including, but not limited to, various species of Talaromyces, Aspergillus, Trichoderma, Neurospora, Penicillium, Fusarium, Humicola, Myceliophthora, Corynascus, Chaetomium, Tolypocladium, Thielavia, Acremonium, Sporotrichum, Thermoascus, and Chrysosporium, are contemplated in the present invention. These are a few of many possible genera of fungi that will be useful sources of enzymes and/or would be suitable as host organisms for producing such enzymes mixtures. Such fungi can be obtained, for instance from various depositories such as the American Type Culture Collection (ATCC), the All Russian Collection of Microorganisms of the Russian Academy of Sciences (VKM), and Centraalbureau voor Schimmelcultures.

Mutant Strains of C. lucknowense

Particular strains of Chrysosporium express proteins in extremely large amounts and natural expression regulating sequences from these strains are of particular interest. These strains have been designated as Chrysosporium strain C1, strain UV13-6, strain NG7C-19 and strain UV18-25. They have been deposited in accordance with the Budapest Treaty with the All Russian Collection (VKM) depository institute in Moscow. The wild type C1 strain was deposited in accordance with the Budapest Treaty with the number VKM F-3500 D, deposit date Aug. 29, 1996, C1 UV13-6 mutant was deposited with number VKM F-3632 D, and deposit date Feb. 9, 1998, C1 NG7c-19 mutant was deposited with number VKM F-3633 D and deposit date Feb. 9, 1998 and C1 UV18-25 mutant was deposited with number VKM F-3631 D and deposit date Feb. 9, 1998.

Preferably an expression-regulating region enabling high expression in the selected host is applied. This can also be a high expression-regulating region derived from a heterologous host, such as are well known in the art. Specific examples of proteins known to be expressed in large quantities and thus providing suitable expression regulating sequences for the invention are without being limited thereto hydrophobin, protease, amylase, xylanase, pectinase, esterase, beta-galactosidase, cellulase (e.g. endo-glucanase, cellobiohydrolase) and polygalacturonase. The high production has been ascertained in both solid state and submerged fermentation conditions. Assays for assessing the presence or production of such proteins are well known in the art.

Heterologous expression-regulating sequences also work efficiently in Chrysosporium as native Chrysosporium sequences. This allows well known constructs and vectors to be used in transformation of Chrysosporium as well as offering numerous other possibilities for constructing vectors enabling good rates of expression in this novel expression and secretion host. As extremely high expression rates for cellulase have been ascertained for Chrysosporium strains, the expression regulating regions of such proteins are particularly preferred.

A nucleic acid construct comprising a nucleic acid expression regulatory region from Chrysosporium lucknowense or a derivative thereof forms a separate embodiment of the invention as does the mutant Chrysosporium strain comprising such regions operably linked to a gene encoding a polypeptide to be expressed. In preferred embodiments, such a nucleic acid construct will be an expression regulatory region from Chrysosporium associated with cellobiohydrolase, endoglucanase, β-glucosidase, and/or xylanase expression.

The invention also covers genetically engineered Chrysosporium strains wherein the sequence that is introduced can be of Chrysosporium origin. Such a strain can, however, be distinguished from natively occurring strains by virtue of for example heterologous sequences being present in the nucleic acid sequence used to transform or transfect the Chrysosporium, by virtue of the fact that multiple copies of the sequence encoding the polypeptide of interest are present or by virtue of the fact that these are expressed in an amount exceeding that of the non-engineered strain under identical conditions or by virtue of the fact that expression occurs under normally non-expressing conditions. The latter can be the case if an inducible promoter regulates the sequence of interest contrary to the non-recombinant situation or if another factor induces the expression than is the case in the non-engineered strain. The invention as defined in the preceding embodiments is not intended to cover naturally occurring Chrysosporium strains. The invention is directed at strains derived through engineering either using classical genetic technologies or genetic engineering methodologies.

A method of production of a recombinant microorganism or plant is also part of the subject invention. The method comprises stably introducing a nucleic acid sequence encoding a heterologous or homologous polypeptide into a microbial strain or plant, the nucleic acid sequence being operably linked to an expression regulating region. Such procedures are for transforming filamentous fungi have been previous reported. In one preferred embodiment, the mutant Chrysosporium lucknowense is derived from UV18-25 (Acc. No. VKM F-3631 D) that has been engineered to overexpress the Xyl II gene.

Genetically Modified Organisms

As used herein, a genetically modified microorganism can include a genetically modified bacterium, yeast, fungus, or other microbe. Such a genetically modified microorganism has a genome which is modified (i.e., mutated or changed) from its normal (i.e., wild-type or naturally occurring) form such that a desired result is achieved (e.g., increased or modified activity and/or production of a least one enzyme or a multi-enzyme product for conversion of lignocellulosic material to fermentable sugars). Genetic modification of a microorganism can be accomplished by using classical strain development and/or molecular genetic techniques. Such techniques known in the art and are generally disclosed for microorganisms, for example, in Sambrook et al., 1989, Molecular Cloning: A Laboratory Manual, Cold Spring Harbor Labs Press. The reference Sambrook et al., ibid., is incorporated by reference herein in its entirety. A genetically modified microorganism can include a microorganism in which nucleic acid molecules have been inserted, deleted or modified (i.e., mutated; e.g., by insertion, deletion, substitution, and/or inversion of nucleotides), in such a manner that such modifications provide the desired effect within the microorganism.

In one aspect of the invention, a genetically modified microorganism can endogenously contain and express an enzyme or a multi-enzyme product for the conversion of lignocellulosic material to fermentable sugars, and the genetic modification can be a genetic modification of one or more of such endogenous enzymes, whereby the modification has some effect on the ability of the microorganism to convert lignocellulosic material to fermentable sugars.

In another aspect of the invention, a genetically modified microorganism can endogenously contain and express an enzyme or a multi-enzyme product for the conversion of lignocellulosic material to fermentable sugars, and the genetic modification can be an introduction of at least one exogenous nucleic acid sequence (e.g., a recombinant nucleic acid molecule), wherein the exogenous nucleic acid sequence encodes at least one additional enzyme useful for the conversion of lignocellulosic material to fermentable sugars and/or a protein that improves the efficiency of the enzyme or multi-enzyme product for the conversion of lignocellulosic material to fermentable sugars. In this aspect of the invention, the microorganism can also have at least one modification to a gene or genes comprising its endogenous enzyme(s) for the conversion of lignocellulosic material to fermentable sugars.

In yet another aspect of the invention, the genetically modified microorganism does not necessarily endogenously (naturally) contain an enzyme or a multi-enzyme product for the conversion of lignocellulosic material to fermentable sugars, but is genetically modified to introduce at least one recombinant nucleic acid molecule encoding at least one enzyme, a multiplicity of enzymes, or a multi-enzyme product for the conversion of lignocellulosic material to fermentable sugars. Such a microorganism can be used in a method of the invention, or as a production microorganism for crude fermentation products, partially purified recombinant enzymes, and/or purified recombinant enzymes, any of which can then be used in a method of the present invention.

Genetically Modified Plants

The invention also contemplates genetically modified plants comprising such genes. The plants may be used for production of the enzymes, or as the lignocellulosic material used as a substrate in the methods of the invention. Methods to generate recombinant plants are known in the art. For instance, numerous methods for plant transformation have been developed, including biological and physical transformation protocols. See, for example, Miki et al., “Procedures for Introducing Foreign DNA into Plants” in Methods in Plant Molecular Biology and Biotechnology, Glick, B. R. and Thompson, J. E. Eds. (CRC Press, Inc., Boca Raton, 1993) pp. 67-88. In addition, vectors and in vitro culture methods for plant cell or tissue transformation and regeneration of plants are available. See, for example, Gruber et al., “Vectors for Plant Transformation” in Methods in Plant Molecular Biology and Biotechnology, Glick, B. R. and Thompson, J. E. Eds. (CRC Press, Inc., Boca Raton, 1993) pp. 89-119.

In certain embodiments of the invention, genetically modified plants that express the enzymes of this invention are obtained by introducing an expression vector into plants based on the natural transformation system of Agrobacterium. See, for example, Horsch et al., Science, 227:1229 (1985). A. tumefaciens and A. rhizogenes are plant pathogenic soil bacteria which genetically transform plant cells. The Ti and Ri plasmids of A. tumefaciens and A. rhizogenes, respectively, carry genes responsible for genetic transformation of the plant. See, for example, Kado, C. I., Crit. Rev. Plant. Sci. 10:1 (1991). Descriptions of Agrobacterium vector systems and methods for Agrobacterium-mediated gene transfer are provided by numerous references, including Gruber et al., supra, Miki et al., supra, Moloney et al., Plant Cell Reports 8:238 (1989), and U.S. Pat. Nos. 4,940,838 and 5,464,763, hereby incorporated by reference in their entirety.

In other embodiments, genetically modified plants are obtained by microprojectile-mediated transformation wherein DNA is carried on the surface of microprojectiles. The expression vector is introduced into plant tissues with a biolistic device that accelerates the microprojectiles to speeds sufficient to penetrate plant cell walls and membranes. Sanford et al., Part. Sci. Technol. 5:27 (1987), Sanford, J. C., Trends Biotech. 6:299 (1988), Sanford, J. C., Physiol. Plant 79:206 (1990), Klein et al., Biotechnology 10:268 (1992).

Another method for physical delivery of DNA to plants contemplated by this invention is sonication of target cells. Zhang et al., Bio Technology 9:996 (1991). Alternatively, liposome or spheroplast fusion have been used to introduce expression vectors into plants. Deshayes et al., EMBO J., 4:2731 (1985), Christou et al., Proc Natl. Acad. Sci. USA 84:3962 (1987). Direct uptake of DNA into protoplasts using CaCh precipitation, polyvinyl alcohol or poly-L-ornithine have also been reported. Hain et al., Mol. Gen. Genet. 199:161 (1985) and Draper et al., Plant Cell Physiol. 23:451 (1982). Electroporation of protoplasts and whole cells and tissues have also been described. Donn et al., In Abstracts of VIIth International Congress on Plant Cell and Tissue Culture IAPTC, A2-38, p. 53 (1990); D'Halluin et al., Plant Cell 4:1495-1505 (1992) and Spencer et al., Plant Mol. Biol. 24:51-61 (1994).

Methods of Using the Enzymes and Mutant Strains of C. lucknowense

This invention also provides methods of enzymatic saccharification of cellulosic materials. Any cellulose containing material can be treated by the enzymes of this invention, non-limiting examples of which include orchard prunings, chaparral, mill waste, urban wood waste, yard waste, municipal waste, logging waste, forest thinnings, short-rotation woody crops, industrial waste, wheat straw, oat straw, rice straw, barley straw, rye straw, flax straw, sugar cane, corn stover, corn stalks, corn cobs, corn husks, prairie grass, gamagrass, foxtail; sugar beet pulp, citrus fruit pulp, seed hulls, cellulosic animal wastes, lawn clippings, cotton, and seaweed.

In certain preferred embodiments, the lignocellulosic materials are pretreated before being exposed to the enzymes or enzyme mixtures of the invention. Generally speaking, the pretreatment can be any procedure that makes the subsequent enzymatic saccharification of the lignocellulosic materials more efficient (i.e., either less time-consuming or less costly). For example, the lignocellulosic material may be pretreated by methods including, but not limited to, exposure to acids, bases, solvents, heat, peroxides, ozone, or some combination thereof prior to enzymatic saccharafication. These pretreatments can also be combined with other forms of processing, such as mechanical shredding, grinding, milling, or rapid depressurization (e.g. steam explosion).

Generally, enzymatic saccharification according to the invention involves using CBH Ia, CBH IIb, EG VI, BGL, Xyl II, or mixtures thereof. One or more of these enzymes may be further combined with other enzymes capable of promoting enzymatic saccharification, which may be derived from C. lucknowense, a mutant strain, or another organism. For example, in one embodiment, the enzymatic saccharification involves an enzyme mixture comprising CBH Ia, CBH Ib, CBH IIb, EG II, EG V, BGL, and Xyl II. In other preferred embodiments, the enzymatic mixture contains a cellobiohydrolase, which may be CBH Ia, CBH Ib, CBH IIa, CBH IIb, and mixtures thereof, with a β-glucosidase such as BGL.

In certain embodiments, the enzyme compositions are artificial enzyme compositions that contain purified forms of CBH Ia, CBH Ib, CBH IIb, EG II, EG VI, BGL, or Xyl II. The purified forms of these enzymes may be used alone on mixed together. In certain preferred embodiments, the selected purified enzymes are present in higher relative amounts than would be the case for the enzyme secretions of the wild type C. lucknowense.

In certain embodiments, the invention provides a mutant strain of C. lucknowense that is capable of expressing CBH Ia, CBH Ib, CBH IIa, CBH IIb, EG II, EG V, EG VI, BGL, or Xyl II, or mixtures thereof in proportions higher than found in the enzyme secretions of the wild-type organism. The secreted enzymes of such a mutant strain of C. lucknowense may serve as a raw source from which purified forms of CBH Ia, CBH Ib, CBH IIa, CBH IIb, EG II, EG V, EG VI, BGL, or Xyl II, can be produced. Alternatively, the secreted enzymes of such a mutant strain may also be applied directly to the cellulosic materials to be saccharified. In particularly preferred embodiments, the cellulosic materials are exposed directly to the mutant strain of C. lucknowense in an environment conducive to the proliferation of the mutant strain of C. lucknowense, such as in a bioreactor. The in situ secretions of CBIa, CBH Ib, CBH IIa, CBH IIb, EG II, EG V, EG VI, BGL, or Xyl II, or mixtures thereof by the mutant strain of C. lucknowense, in proportions higher than found in the enzyme secretions of the wild-type organism, lead to enhanced in situ saccharification of the cellulosic material.

Following enzymatic treatment by the inventive enzymatic compositions of the invention, the fermentable sugar that is produced can be exposed to microorganisms, either naturally occurring or genetically engineered, that are capable of fermenting the sugar to produce ethanol or some other value-added fermentation product. Preferably, substantially all of the glucose is converted to ethanol, which may be subsequently used as a fuel, solvent, or chemical reactant. In preferred embodiments, the ethanol is used as a fuel for powering transportation vehicles, non-limiting examples of which include cars, trucks, buses, mopeds and motorcycles. Other potential fermentation products from glucose include, but are not limited to, biofuels (including ethanol); lactic acid; plastics; specialty chemicals; organic acids, including citric acid, succinic acid and maleic acid; solvents; animal feed supplements; pharmaceuticals; vitamins; amino acids, such as lysine, methionine, tryptophan, threonine, and aspartic acid; industrial enzymes, such as proteases, cellulases, amylases, glucanases, lactases, lipases, lyases, oxidoreductases, and transferases; and chemical feedstocks.

EXAMPLES

Example 1

Enzyme Isolation

Culture filtrates produced by the C. lucknowense mutant strains were used for isolation of individual enzymes. Commercial preparation of NCE-L600 (C. lucknowense) were from Dyadic International, Inc., USA.

Highly purified BGL (cellobiase) from Aspergillus japonicus was obtained from a commercial preparation, having specific cellobiase activity 50 U mg⁻¹ protein (pH 5.0, 40° C.), and was used in the experiments on hydrolysis of insoluble cellulose.

Example 2

Enzyme Purification

The enzyme purification was carried out by chromatography on a Pharmacia FPLC system (Sweden). Cellobiohydrolases and endoglucanases BGL and Xyl II were isolated from a C. lucknowense UV18-25 culture filtrate. BGL and Xyl II (xylanase II) were isolated from culture filtrates produced by the C. lucknowense UV18ΔCbh1#10 and Xyl2-18 mutant strains, respectively.

In all cases, the first purification stage was anion-exchange chromatography on a Source 15Q column (40 ml volume). The column was equilibrated with 0.02 M Bis-Tris-HCl buffer, pH 6.8. The initial culture filtrate was preliminarily desalted and transferred into the starting buffer by gel-filtration on Acrylex P4 (Reanal, Hungary). The sample (400 mg of protein) was applied to the Source 15Q column, and the elution was carried out with a gradient of 0-1 M NaCl at a flow rate of 10 ml min⁻¹.

The first protein fraction after the Source 15Q, eluted at 0.05 M NaCl and having high Avicelase activity, was subjected to hydrophobic interaction chromatography on a Source 15 Isopropyl column (Pharmacia, Sweden). The column was equilibrated with 1.7 M ammonium sulfate in 50 mM Na-acetate buffer, pH 5.0. Proteins were eluted with a reverse linear gradient of 1.7-0 M ammonium sulfate at a flow rate of 4 ml min⁻¹. The protein fraction with the highest activity against Avicel (eluting at a salt concentration of 0.30-0.35 M) contained the homogeneous protein with a molecular mass of 70 kDa (CBH IIb, see FIG. 1).

The protein fraction after the Source 15Q, eluted at 0.22 M NaCl and having the activity against Avicel and p-NP-β-D-cellobioside, was further purified by chromatofocusing on a Mono P HR 5/20 column (Pharmacia, Sweden). The column was equilibrated with 0.025 M Na-formate buffer, pH 4.0. Proteins were eluted with a gradient of pH 4.5-3.0 (using Polybuffer 74) at a flow rate of 0.5 ml⁻¹. Homogeneous 60 kDa CBH Ib was obtained as a result of chromatofocusing (FIG. 1).

The two newly isolated cellobiohydrolases are homogeneous according to the data of SDS-PAGE and isoelectrofocusing (FIG. 1), their molecular masses were found to be 60 and 70 kDa, pI 3.8 and 5.6, respectively. Peptide mass fingerprinting using MALDI-TOF mass spectrometry (data not shown) indicated that these proteins were different from the above-mentioned cellobiohydrolases (Ce16A and Ce17A) as well as from other C. lucknowense enzymes previously isolated. Subsequent de novo sequencing of tryptic peptides from the new cellobiohydrolases, using tandem TOF/TOF mass spectrometry (MS/MS), followed by the BLAST search in the SWISS-PROT (UniProtKB) database showed that the 60 kDa and 70 kDa proteins display sequence similarity to cellobiohydrolases from the GH families 7 and 6 (Table 1, see classification into families in http://afmb.cnrs-mrs.fr/CAZY/). So, they were classified as Ce17B (CBH Ib) and Ce16B (CBH IIb), respectively. Thus, the C. lucknowense fungus secretes at least four cellobiohydrolases encoded by different genes, two of them belonging to the glycosyl hydrolase family 6 (GH6) and two other enzymes—to the GH7 family (Table 2). The molecules of the CBH Ia (Ce17A) and CBH IIb (Ce16B) represent typical cellulases consisting of a catalytic domain and CBM connected by a flexible peptide linker. The molecules of CBH Ib (Ce17B) and CBH IIa (Ce16A) consist of only the catalytic domains (they lack CBM). It should be noted that the most studied fungus T. reesei has only two cellobiohydrolases: I (Ce17A) and II (Ce16A). Other fungi, such as Humicola insolens, also secrete two cellobiohydrolases (Ce17A and Ce16A), while Phanerochaete chrysosporium produces at least seven different cellobiohydrolases, of which six enzymes belong to the GH7 family. All the enzymes mentioned, except for the P. chrysosporium CBH 1-1 (Ce17A), possess CBM.

The BGL was isolated from the protein fraction after the Source 15Q (eluted at 0.10 M NaCl) containing the highest activity against p-NP-β-D-glucopyranoside and cellobiose. The fraction was subjected to hydrophobic interaction chromatography as described above, the homogeneous BGL with a molecular mass of 106 kDa and pI 4.8 was eluted at 1.3 M of ammonium sulfate. The specific activity of the BGL toward p-NP-β-D-glucopyranoside and cellobiose was found to be 11 and 26 U mg⁻¹ of protein, respectively (40° C., pH 5.0). Purified BGL had optimum activity at pH 4.0 and retained >50% of activity in the range of pH 2.5-6.5. The temperature optimum was 40° C. After heating for three hours, the enzyme retained 10% activity at 60° C., 64% at 50° C., and 100% at 40° C. The enzyme was highly active against cellobiose, gentiobiose, and laminarobiose as substrates. Weak activity was also observed using sophorose, cellotriose, cellotetraose, cellopentaose, and cellohexaose as substrates. No activity was observed with lactose or tregalose as substrates.

The homogeneous Xyl II (24 kDa, pI 7.9) was obtained after anion-exchange chromatography followed by hydrophobic interaction chromatography as described above and gel-filtration on a Superose 12 HR 10/30 column (Pharmacia, Sweden). Elution at the last chromatographic stage was performed with 0.1 M Na-acetate buffer, pH 5.0, at a flow rate of 0.3 ml min⁻¹. The Xyl II had specific xylanase activity of 395 U mg⁻¹ of protein (50° C., pH 5.0, birchwood xylan as a substrate). The enzyme had a pH optimum of 6.0 and a temperature optimum of 70° C. Xyl II was highly specific for xylan as substrate, with no activity against carboxymethylcellulose (CMC) or barley β-glucan.

The C. lucknowense CBH Ia (65 kDa), CBH IIa (43 kDa), EG II (51 kDa), EG V (25 kDa), EG VI (47 kDa) were purified as described elsewhere (see, Gusakov A V, Sinitsyn A P, Salanovich T N, Bukhtojarov F E, Markov A V, Ustinov B B, van Zeijl C, Punt P, Burlingame R. “Purification, cloning and characterisation of two forms of thermostable and highly active cellobiohydrolase I (Ce17A) produced by the industrial strain of Chrysosporium lucknowense” Enzyme Microb Technol 2005; 36:57-69; Bukhtojarov F E, Ustinov B B, Salanovich T N, Antonov A I, Gusakov A V, Okunev O N, Sinitsyn A P. “Cellulase complex of the fungus Chrysosporium lucknowense: isolation and characterization of endoglucanases and cellobiohydrolases”, Biochemistry (Moscow) 2004; 69:542-51.

The enzyme purity was characterized by SDS-PAGE and isoelectrofocusing. SDS-PAGE was carried out in 12% gel using a Mini Protean II equipment (Bio-Rad Laboratories, USA). Isoelectrofocusing was performed on a Model 111 Mini IEF Cell (Bio-Rad Laboratories, USA). Staining of protein was carried out with Coomassie Blue.

Example 3

MALDI-TOF and Tandem TOF/TOF Mass Spectrometry of Peptides

The in-gel tryptic digestion of the protein bands after the SDS-PAGE was carried out essentially as described by Smith (Smith B E. Protein sequencing protocols. Totowa: Humana Press; 1997). Trypsin (Promega, modified, 5 μg/mL) in 50 mM NH₄HCO₃ was used for a protein digestion. The resulting peptides were extracted from a gel with 20% aqueous acetonitrile containing 0.1% trifluoroacetic acid and subjected to MALDI-TOF MS (see, James P. (Ed.) Proteome research: mass spectrometry. Berlin: Springer-Verlag; 2001.) Selected peptides from the mass spectra of the tryptic digests of the CBH Ib and IIb were analyzed by tandem mass spectrometry in order to determine their sequences de novo. Ultraflex TOF/TOF mass spectrometer (Bruker Daltonik Gmbh, Germany) was used in the MS experiments.

Example 4

Enzyme Activity Assays

CMCase activity was measured by assaying reducing sugars released after 5 min of enzyme reaction with 0.5% carboxymethylcellulose (CMC, medium viscosity, Sigma, USA) at pH 5.0 and 50° C. (Sinitsyn A P, Chemoglazov V M, Gusakov A V. “Methods of investigation and properties of cellulolytic enzymes” (in Russian), Biotechnology Series, v. 25. Moscow: VINITI Press; 1990). Enzyme activities against barley β-glucan (Megazyme, Australia) and birchwood xylan (Sigma, USA) were determined in the same way as the CMCase activity, except the incubation time was 10 min. Avicelase activity was determined by analysing reducing sugars released after 60 min of enzyme reaction with 5 mg ml⁻¹ Avicel PH 105 (Serva, Germany) at pH 5.0 and 40° C. Reducing sugars were analysed by the Somogyi-Nelson method (Sinitsyn A P, Chernoglazov V M, Gusakov A V, “Methods of investigation and properties of cellulolytic enzymes” (in Russian), Biotechnology Series, v. 25. Moscow: VINITI Press; 1990; Somogyi M., “Notes on sugar determination” J Biol Chem 1952; 195:19-23. Filter paper activity (FPA) was determined as recommended by Ghose (Ghose T K. “Measurement of cellulase activities”, Pure Appl Chem 1987; 59:257-68).

Activities against p-NP-β-D-glucopyranoside, p-NP-β-D-cellobioside and p-NP-β-D-lactoside (Sigma, USA) were determined at pH 5.0 and 40° C. as described elsewhere (Gusakov A V, Sinitsyn A P, Salanovich T N, Bukhtojarov F E, Markov A V, Ustinov B B, van Zeijl C, Punt P, Burlingame R. “Purification, cloning and characterisation of two forms of thermostable and highly active cellobiohydrolase I (Ce17A) produced by the industrial strain of Chrysosporium lucknowense”, Enzyme Microb Technol 2005; 36:57-69).

Cellobiase activity was assayed at pH 5.0 and 40° C. by measuring the initial rate of glucose release from 2 mM cellobiose by the glucose oxidase-peroxidase method (Sinitsyn A P, Chernoglazov V M, Gusakov A V, “Methods of investigation and properties of cellulolytic enzymes” (in Russian), Biotechnology Series, v. 25. Moscow: VINITI Press; 1990).

All activities were expressed in International Units, i.e. one unit of activity corresponded to the quantity of enzyme hydrolysing one μmol of substrate or releasing one μmol of reducing sugars (in glucose equivalents) per one minute.

Example 5

Enzymatic Hydrolysis of Cellulosic Substrates

The enzymatic hydrolysis of cellulosic substrates was carried out at pH 5.0 under magnetic stirring. Avicel PH 105 (Serva, Germany), cotton pretreated with acetone-ethanol mixture (1:1) for two days in order to remove wax from the surface of cellulose fibres, and Douglas fir wood pretreated by organosolv were used as substrates.

The experiments on progress kinetics of Avicel hydrolysis by purified individual cellobiohydrolases and experiments on synergistic interaction between C. lucknowense cellulases (with cotton as a substrate) were carried out at 40° C. The substrate concentration in those experiments was 5 mg ml⁻¹. In order to eliminate the effect of product (cellobiose) inhibition on the kinetics and to convert all cellooligosaccharides to glucose, the hydrolysis was carried out in the presence of purified BGL (cellobiase) from A. japonicus, which was extra added to the reaction system in excessive quantity (0.5 U ml⁻¹).

The experiments on enzymatic saccharification of Avicel, cotton, and pretreated Douglas fir wood by combinations of purified C. lucknowense enzymes and crude multienzyme preparations were carried out at 50° C. The concentration of Avicel and pretreated wood in those experiments was 50 mg ml⁻¹, while the concentration of cotton was 25 mg ml⁻¹.

A typical experiment was carried out in the following way. A weighed amount of dry cellulosic substrate was placed into a 2-ml plastic test tube, then 0.5-1 ml of 0.05 M Na-acetate buffer, containing 1 mM NaN₃ to prevent microbial contamination, was added, and the substrate was soaked in the buffer for 1 h. Then, the tube was placed into a thermostated water bath, located on a magnetic stirrer, and suitably diluted enzyme solution in the same buffer was added to the substrate suspension in order to adjust the total volume of the reaction system to 2 ml and to start the hydrolysis. The tube was hermetically closed with a lid, and the hydrolysis was carried out with magnetic stirring. At defined times in the reaction, an aliquot of the suspension (0.05-0.1 ml) was taken, diluted, centrifuged for 3 min at 15000 rpm, and the concentrations of glucose and reducing sugars in the supernatant were determined by the glucose oxidase-peroxidase and Somogyi-Nelson methods. In those cases, when glucose was a single product of the reaction, the degree of substrate conversion (for Avicel and cotton, which represented pure cellulosic substrates) was calculated using the following equation:

$\mathrm{Conversion}\left(\%\right)=\frac{\mathrm{Glucose}\mathrm{concentration}\left(\mathrm{mg}{\mathrm{ml}}^{-1}\right)\times 100\%}{\mathrm{Initial}\mathrm{substrate}\mathrm{concentration}\left(\mathrm{mg}{\mathrm{ml}}^{-1}\right)\times 1.11}$

The kinetic experiments were carried out in duplicates. Protein concentration was the measure of enzyme loading in the reaction system. In the case of purified enzymes, the protein concentration was calculated from the UV absorption at 280 nm using enzyme extinction coefficients predicted by the ProtParam tool (http://www.expasy.ch/tools/protparam.html). For crude multienzyme preparations, the protein concentration was determined by the Lowry method using bovine serum albumin as a standard.

The CBH Ib and IIb displayed maximum activity at pH 4.7 and 5.0. Both enzymes were stable during 24 h incubation at pH 5.0 and 50° C. Study of the enzyme adsorption on Avicel, carried out at pH 5.0 and 6° C., revealed that only the CBH IIb has CBM. After incubation of the CBH Ib and IIb (1 mg ml⁻¹) with Avicel (25 mg ml⁻¹) for 30 min on stirring the degree of protein adsorption was 65 and 99%, respectively. It should be noted that the adsorption degree of the catalytic domain of the C. lucknowense CBH Ia was 59% under the same conditions, while that for the full size C. lucknowense CBH Ia (an enzyme with CBM) was 89%.

The CBH IIb had a high activity against Avicel and very low CMCase activity, while the activity toward synthetic p-nitrophenyl derivatives of disaccharides was completely absent (Table 2). The CBH Ib displayed lower Avicelase activity, but hydrolysed p-NP-β-D-cellobioside and p-NP-β-D-lactoside, which is typical for family 7 cellulases. For a comparison, specific activities of previously isolated C. lucknowense cellobiohydrolases (now named as CBH Ia and CBH IIa) are also given in Table 2.

FIG. 2 shows the progress kinetics of Avicel hydrolysis by the all purified C. lucknowense cellobiohydrolases, where the enzymes were equalized by protein concentration (0.1 mg ml⁻¹). In order to eliminate the effect of product (cellobiose) inhibition on the kinetics, the hydrolysis was carried out in the presence of purified BGL (cellobiase) from A. japonicus, added to the reaction system in excessive quantity (0.5 U ml⁻¹).

The highest hydrolysis rate amongst a few cellobiohydrolases tested, including three other C. lucknowense enzymes (CBH Ia, Ib, Ha) was observed in the case of C. lucknowense CBH IIb: 3.2 mg ml⁻¹ of glucose, i.e. 58% cellulose conversion was achieved after 5 days of hydrolysis (see FIG. 2). The C. lucknowense CBH Ia (which has a CBM) was notably less effective (the yield of glucose after 5 days was 2.5 mg ml⁻¹, which corresponded to the cellulose conversion degree of 46%, respectively). As expected, the C. lucknowense cellobiohydrolases without CBM (CBH Ib and IIa) had the lowest ability to hydrolyse Avicel: only 23 and 21% cellulose conversion was achieved after the same time of reaction.

Both C. lucknowense cellobiohydrolases having a CBM (Ia and IIb) displayed a pronounced synergism with three major endoglucanases from the same fungus (EG II, EG V, EG VI) in hydrolysis of cotton as well as a strong synergy with each other (Table 3). In these studies, the concentration of cotton was 5 mg ml⁻¹, the CBH concentration was 0.15 mg ml⁻¹ in all cases, while the EG concentration was always 0.05 mg ml⁻¹. In order to eliminate the effect of product inhibition on the kinetics and to convert the intermediate oligosaccharides to glucose, the hydrolysis was carried out in the presence of purified BGL from A. japonicus, added to the reaction system in excessive quantity (0.5 U ml⁻¹). The experiments were carried out at pH 5.0 and 40° C. for 140 h.

As seen from Table 3, individual cellobiohydrolases, CBH Ia and CBH IIb, and the individual endoglucanases, did not completely hydrolyze cotton under the conditions tested. The CBH IIb provided the highest glucose yield after 140 h of hydrolysis: 1.18 mg ml⁻¹, which corresponded to the substrate conversion degree of 21%. However, when either cellobiohydrolase was incubated with endogluacanase, a pronounced synergism was observed. The highest glucose yields (4.1-4.7 mg ml⁻¹) were achieved with combinations of CBH Ia or CBH IIb with EG II, the coefficient of synergism being varied in the range of 2.6-2.8. A strong synergism (K_syn=2.75) was also observed between CBH Ia and CBH IIb. In fact, the combination of two cellobiohydrolases (1:1 by weight) with BGL provided practically complete conversion (98.6%) of cotton cellulose to glucose after 140 h of hydrolysis.

As an example, the progress kinetics of cotton hydrolysis by combinations of CBH IIb with other C. lucknowense enzymes are shown in FIG. 3, where real experimental data are shown with open symbols (continuous curves) while the theoretical sums of glucose concentrations obtained under the action of individual enzymes are shown with filled symbols (dotted lines). Glucose yields obtained after 140 h of cotton hydrolysis under the action of individual cellobiohydrolases and endoglucanases and their combinations are summarized in Table 3. The coefficient of synergism (K_syn) was calculated as a ratio of experimental glucose concentration (column 2 of Table 3) to the theoretical sum of glucose concentrations (column 3).

Using four purified C. lucknowense enzymes (CBH Ia and IIb, EG II, BGL), an artificial cellulase complex was constructed (C.l. combination #1) that demonstrated an extremely high ability to convert different cellulosic substrates to glucose (FIGS. 4-6). This multienzyme composition was notably more effective in hydrolysis of pure crystalline cellulose (cotton and Avicel) than the crude C. lucknowense multienzyme preparation NCE-L600. In 72-h hydrolysis of a lignocellulosic substrate (Douglas fir wood pretreated by organosolv), the C.l. combination #1 was also very effective in cellulose hydrolysis.

In C. lucknowense combination #1, the enzyme consisted of the two cellobiohydrolases CBH Ia and CBH Ib, and the endoglucanase EG II, the enzymes with strong adsorption ability on crystalline cellulose (the molecules of these enzymes have CBM). The activity of tightly adsorbed cellulases is gradually decreased during in the course of hydrolysis of insoluble cellulose as a result of the enzyme limited mobility along the substrate surface or unproductive binding (so called pseudoinactivation). Without wishing to be bound by theory, it is believed that there may exist a synergism between tightly and loosely adsorbed cellulases wherein loosely binding cellulases (enzymes without CBM) may destroy obstacles hindering the processive action of the tightly adsorbed cellobiohydrolases, thus helping them to move to the next cellulose reactive sites. The total protein concentration in the reaction system was 0.5 mg ml⁻¹. The composition of the multienzyme composition (C.l. combination #1) was the following: 0.2 mg ml⁻¹ of CBH Ia+0.2 mg ml⁻¹ of CBH IIb+0.08 mg ml⁻¹ of EG II+0.02 mg ml⁻¹ of BGL. Avicel (50 mg ml⁻¹) and cotton (25 mg ml⁻¹) were used as substrates representing pure crystalline cellulose in these experiments. Sample of Douglas fir wood pretreated by organosolv (50 mg ml⁻¹) was taken as an example of real lignocellulosic feedstock that may be used for bioconversion to ethanol. A crude C. lucknowense multienzyme cellulase preparation NCE L-600 (diluted so that the protein concentration in the reaction system would also be 0.5 mg ml⁻¹) was taken for a comparison in these studies. The hydrolysis experiments with them were carried out also in the presence of extra added A. japonicus BGL (0.5 U ml⁻¹).

The progress kinetics of cotton, Avicel and Douglas fir hydrolysis by different cellulase multienzyme preparations are shown in FIGS. 4-6. It should be noted that in all cases, the concentrations of glucose and reducing sugars after 24-72 h of hydrolysis in a concrete experiment were practically the same, i.e. glucose made up >96% of the total soluble sugars. So, the glucose yield can be taken as reliable criterion in comparison of the hydrolytic efficiency of different multienzyme samples.

In hydrolysis of cotton (FIG. 4), the combination #1 of purified C. lucknowense enzymes provided much higher glucose yield after 72 h of the reaction (23.4 mg ml⁻¹, i.e. 84% degree of substrate conversion) than the 4.2 mg ml⁻¹ exhibited by (NCE-L600). In hydrolysis of Avicel (FIG. 5), the C.l. combination #1 was also superior (45.0 mg ml⁻¹ of glucose, or 81% substrate conversion after 72 h of hydrolysis). In the case of pretreated Douglas fir (FIG. 6), the C.l. combination #1 was also effective (28.8 mg ml⁻¹ glucose, 63% conversion after 72 hours).

Unlike Avicel and cotton, the pretreated wood sample contained not only cellulose (˜85%) but also lignin (13%) and hemicellulose (2%). The artificial C. lucknowense four-enzyme combination #1 was composed of only cellulases; all of them, except for the BGL, having CBM. All other multienzyme samples possessed not only cellulase but also xylanase and other types of carbohydrase activity, i.e. they contained non-cellulase accessory enzymes. This may explain relatively lower efficiency of the C.l. combination #1 on pretreated Douglas fir compared to the P. verruculosum #151 preparation (FIG. 6).

In one set of experiments (FIG. 7), the pretreated wood sample was hydrolysed by different compositions of purified C. lucknowense enzymes, to which cellulases lacking a CBM were included (EG V or EG V in combination with CBH Ib). The total protein concentration in the reaction system was maintained at the same level of 0.5 mg ml⁻¹ (Table 5). Indeed, two C.l. combinations (#3 and #4), containing weakly adsorbed enzymes, provided a notable enhancement of the glucose yield after 72 h of the enzymatic reaction in comparison with the C.l. combination #1.

In two experiments, the highly active C. lucknowense Xyl II (Xyn11A) was added to the above-mentioned four enzymes (C.l. combinations #2 and #4). Since a synergism between tightly and loosely adsorbed cellulases has been described [38], EG V or EG V together with CBH Ib (both enzymes have lack CBM) were used in the C.l. combinations #3 and #4.

As can be seen from FIG. 7, the initial rate of glucose formation decreased sequentially from C.l. combination #1 to combination #4, however the glucose yield after 2-3 days of hydrolysis increased in the same sequence. The Xyl II demonstrated only slight positive effect on the glucose yield, while the EG V or EG V together with CBH Ib provided a very notable increase in the product concentration after 72 h hydrolysis of wood (37 and 41 mg ml⁻¹, respectively) compared to the C.l. combination #1 (29 mg ml⁻¹), i.e. the combinations #3 and #4 performed much better than all crude multienzyme samples (FIG. 6).

The low performance of the crude C. lucknowense preparation (NCE-L600) in hydrolysis of different cellulosic substrates (FIGS. 4-6) deserves a special attention. Without wishing to be bound by theory, it may be explained by the low total content of different cellobiohydrolases in the NCE-L600 (35-40% of the total protein content). Moreover, two of four C. lucknowense cellobiohydrolases (Ib and IIa) lack CBM, while two other enzymes (CBH Ia and IIb) also partially lose the CBM during the course of fermentation. The CBM absence in major part of cellobiohydrolases from the NCE-L600 may lead to the lower activity of the crude preparation toward crystalline cellulose.

TABLE 1
Identification of peptides in the isolated
C. lucknowense proteins using MALDI-TOF MS/MS
				UniProtKB
Enzyme	m/z	Peptidea	BLAST identificationb	No.
Protein 60	1133.6	HEYGTNIGSR	118 HEYGTNIGSR 127	O94093
kDa			(cbh1.2 Humicola grisea - GH7)
	1829.9	MGNQDFYGPGLTVDTS	291 LGNTDFYGPGLTVDT 305	Q9UVS8
		K	(cbhB Aspergillus niger - GH7)
Protein 70	1061.4	YPANDYYR	127 ANNYYR 132	Q9C1S9
kDa			(Avicelase 2 Humicola insolens -
			GH6)
	1990.0	HYIEAFSPLLNSAGFPAR	367 KYIEAFSPLLNAAGFPA 383	Q872J7
			(CBH II Neurospora crassa - GH6)
	2073.5	LWQPTGQQQWGDWCN	381 QPTGQQQWGDWCNV 394	P07987
		VK	(CBH II T. reesei - GH6)
aSince the MS/MS can not distinguish between Leu and Ile residues (they have the same masses), there may be ambiguity in the appropriate positions of the identified peptides.
bResidues conserved in the C. lucknowense enzymes are shown in bold.

TABLE 2
Specific activities (U mg−1 of protein) of purified cellobiohydrolases from
C. lucknowense toward different substrates at pH 5.0 and 40° C.
	Mol.	Cat.				Barley
	mass	domain	CBM			β-	p-NP-β-D-	p-NP-β-D-
Enzyme	(kDa)	designation	presence	Avicel	CMCa	glucana	cellobioside	lactoside
CBH Ia	65	Cel7A	Yes	0.21	0.1	<0.1	0.021	0.12
CBH Ib	60	Cel7B	No	0.12	0.3	<0.1	0.020	0.09
CBH IIa	43	Cel6A	No	0.08	1.1	2.0	0	0
CBH IIb	70	Cel6B	Yes	0.22	0.2	0.2	0	0
aActivity was determined at 50° C.

TABLE 3
Synergism between C. lucknowense cellulases in hydrolysis of cotton
cellulose (5 mg ml−1) at pH 5.0 and 40° C. in the presence of 0.5 U ml−1
of A. japonicus BGL. In all cases the CBH concentration was
0.15 mg ml−1, the EG concentration was 0.05 mg ml−1.
	Glucose concentration	Glucose concentration
	after 140 h,	after 140 h,
Enzyme	experimental (mg ml−1)	theoreticala (mg ml−1)	Ksyn
CBH Ia	0.81	—	—
CBH IIb	1.18	—	—
EG II	0.64	—	—
EG V	0.70	—	—
EG VI	0.40	—	—
CBH Ia + EG II	4.05	1.45	2.79
CBH Ia + EG V	3.68	1.51	2.44
CBH Ia + EG VI	3.93	1.21	3.25
CBH IIb + EG II	4.72	1.82	2.59
CBH IIb + EG V	3.81	1.88	2.03
CBH IIb + EGVI	4.05	1.58	2.56
CBH Ia + CBH IIb	5.47	1.99	2.75
aCalculated as a sum of glucose concentrations obtained under the action of individual enzymes.

TABLE 4
Specific activities (U mg−1 of protein) of multienzyme preparations
toward different substrates at pH 5.0 and 50° C.
	Protein
Prep-	(mg ml−1	Filter
aration	or mg g−1)	paper	CMC	Xylan	Cellobiosea
NCE-L600	45	0.25	12.2	4.8	0.07
C.l. combin-	1000	1.10	6.6	0	1.05
ation #1
aActivity was determined at 40° C.

TABLE 5
Composition of artificial multienzyme combinations based on purified C. lucknowense
enzymes and yields of glucose after 72-h hydrolysis of pretreated Douglas fir wood (50
mg ml−1), pH 5.0, 50° C. The total protein concentration in the reaction system was 0.5
mg ml−1, the concentration of each component and glucose yields are given in mg ml−1.
Combination	CBH Ia	CBH Ib	CBH IIb	EG II	EG V	BGL	Xyl II	Glucose yield
#01	0.2	0	0.2	0.08	0	0.02	0	28.8
#02	0.2	0	0.2	0.07	0	0.02	0.01	30.1
#03	0.2	0	0.2	0.04	0.04	0.02	0	37.3
#04	0.1	0.1	0.2	0.03	0.04	0.02	0.01	41.0

Claims

1. A method of producing a fermentation product or a starting material for a fermentation product from a fermentable sugar, wherein said method comprises: (a) providing an enzyme formulation, wherein said enzyme formulation comprises at least two enzymes selected from the group consisting of EG II (SEQ ID NO. 10) and BGL (SEQ ID NO 12); (b) applying said enzyme formulation to lignocellulosic material to produce a fermentable sugar; and (c) fermenting said fermentable sugar to produce a fermentation product.

2. The method according to claim 1, wherein the fermentable sugar is selected from the group consisting of glucose, xylose, arabinose, galactose, mannose, rhamnose, sucrose and fructose.

3. The method according to claim 1, wherein the lignocellulosic material is selected from the group consisting of orchard prunings, chaparral, mill waste, urban wood waste, municipal waste, logging waste, forest thinnings, short-rotation woody crops, industrial waste, wheat straw, oat straw, rice straw, barley straw, rye straw, flax straw, soy hulls, rice hulls, rice straw, corn gluten feed, oat hulls, sugar cane, corn stover, corn stalks, corn cobs, corn husks, prairie grass, gamagrass, foxtail; sugar beet pulp, citrus fruit pulp, seed hulls, cellulosic animal wastes, lawn clippings, cotton, seaweed, trees, shrubs, grasses, wheat, wheat straw, sugar cane bagasse, corn, corn husks, corn kernel, fiber from kernels, products and by-products from wet or dry milling of grains, municipal solid waste, waste paper, yard waste, herbaceous material, agricultural residues, forestry residues, municipal solid wastes, waste paper, pulp, paper mill residues, branches, bushes, canes, corn, corn husks, energy crops, forests, fruits, flowers, grains, grasses, herbaceous crops, leaves, bark, needles, logs, roots, saplings, shrubs, switch grasses, trees, vegetables, fruit peels, vines, sugar beet pulp, wheat midlings, oat hulls, hard and soft woods, organic waste materials generated from agricultural processes, forestry wood waste, or combinations thereof.

4. The method according to claim 1, wherein said fermentation product is a biofuel.

5. The method according to claim 1, wherein said fermentation product is selected from the group consisting of lactic acid, organic acids, animal feed supplements, pharmaceuticals, vitamins, amino acids, industrial enzymes, and chemical feedstocks.

6. The method according to claim 4, wherein said combustible fermentation product is an alcohol.

7. The method according to claim 1, wherein the lignocellulosic material is subjected to a pretreatment prior to being exposed to enzymes; wherein said pretreatment comprises exposing the lignocellulosic biomass to an acid, base, solvent, heat, peroxide, ozone, mechanical shredding, grinding, milling, rapid depressurization, or a combination thereof.

8. The method according to claim 7, wherein said solvent is an acetone/ethanol mixture or organosolv.

9. A method for degrading a lignocellulo sic material to fermentable sugars, said method comprising contacting the lignocellulosic material with an effective amount of a multi-enzyme product derived from a microorganism, to produce at least one fermentable sugar wherein at least one of enzyme in the multi-enzyme product is selected from the group consisting of EG II (SEQ ID NO. 10) and BGL (SEQ ID NO. 12).

10. A method of producing energy from a fermentable sugar, said method comprising (a) providing an enzyme formulation, wherein said enzyme formulation comprises at least one enzyme selected from the group consisting of EG II (SEQ ID NO. 10) and BGL (SEQ ID NO 12); (b) applying said enzyme formulation to lignocellulosic material to produce a fermentable sugar; (c) fermenting said fermentable sugar to produce a combustible fermentation product; (d) combusting said combustible fermentation product to produce energy.

11. The method according to claim 10, wherein the fermentable sugar is selected from the group consisting of glucose, xylose, arabinose, galactose, mannose, rhamnose, sucrose and fructose.

12. The method according to claim 10, wherein the lignocellulosic material is selected from the group consisting of orchard prunings, chaparral, mill waste, urban wood waste, municipal waste, logging waste, forest thinnings, short-rotation woody crops, industrial waste, wheat straw, oat straw, rice straw, barley straw, rye straw, flax straw, soy hulls, rice hulls, rice straw, corn gluten feed, oat hulls, sugar cane, corn stover, corn stalks, corn cobs, corn husks, prairie grass, gamagrass, foxtail; sugar beet pulp, citrus fruit pulp, seed hulls, cellulosic animal wastes, lawn clippings, cotton, seaweed, trees, shrubs, grasses, wheat, wheat straw, sugar cane bagasse, corn, corn husks, corn kernel, fiber from kernels, products and by-products from wet or dry milling of grains, municipal solid waste, waste paper, yard waste, herbaceous material, agricultural residues, forestry residues, municipal solid wastes, waste paper, pulp, paper mill residues, branches, bushes, canes, corn, corn husks, energy crops, forests, fruits, flowers, grains, grasses, herbaceous crops, leaves, bark, needles, logs, roots, saplings, shrubs, switch grasses, trees, vegetables, fruit peels, vines, sugar beet pulp, wheat midlings, oat hulls, hard and soft woods, organic waste materials generated from agricultural processes, forestry wood waste, or combinations thereof.

13. The method according to claim 10, wherein said combustible fermentation product is an alcohol.

14. The method according to claim 10, wherein the lignocellulosic material is subjected to a pretreatment prior to being exposed to enzymes; wherein said pretreatment comprises exposing the lignocellulosic biomass to an acid, base, solvent, heat, peroxide, ozone, mechanical shredding, grinding, milling, rapid depressurization, or a combination thereof.

15. The method according to claim 14, wherein said solvent is an acetone/ethanol mixture or organosolv.