# Patent

## Title
Methods for increasing hydrolysis of cellulosic material

## Abstract

The present invention relates to methods for pretreating a cellulosic material, methods for degrading or converting a cellulosic material, methods for producing a fermentation product, and methods of fermenting a cellulosic material under anaerobic conditions.

## Background
CROSS-REFERENCE TO RELATED APPLICATION
This application claims the benefit of U.S. Provisional Application No. 61/139,412, filed Dec. 19, 2008, which application is incorporated herein by reference.


REFERENCE TO A SEQUENCE LISTING
This application contains a Sequence Listing filed electronically by EFS, which is incorporated herein by reference.
BACKGROUND OF THE INVENTION
1. Field of the Invention
The present invention relates to methods for increasing hydrolysis of cellulosic material with an enzyme composition.
2. Description of the Related Art
Cellulose is a polymer of the simple sugar glucose linked by beta-1,4-bonds. Many microorganisms produce enzymes that hydrolyze beta-linked glucans. These enzymes include endoglucanases, cellobiohydrolases, and beta-glucosidases. Endoglucanases digest the cellulose polymer at random locations, opening it to attack by cellobiohydrolases. Cellobiohydrolases sequentially release molecules of cellobiose from the ends of the cellulose polymer. Cellobiose is a water-soluble beta-1,4-linked dimer of glucose. Beta-glucosidases hydrolyze cellobiose to glucose.
It is well known in the art that oxidation of biomolecules such as DNA, lipids, or protein is a significant issue in biological systems. Consequently, removal or exclusion of reactive oxygen species may improve the performance of cellulose-hydrolyzing enzyme systems.
Hydrolysis of cellulosic material, e.g., lignocellulose, by an enzyme composition can be reduced by oxidative damage to components of the enzyme composition and/or oxidation of the cellulosic material by, for example, molecular oxygen.
The present invention provides methods for increasing hydrolysis of cellulosic materials with an enzyme composition.
SUMMARY OF THE INVENTION
The present invention relates to methods for pretreating a cellulosic material, comprising: pretreating the cellulosic material under anaerobic conditions.
The present invention also relates to methods for degrading or converting a cellulosic material, comprising: treating the cellulosic material with an enzyme composition under anaerobic conditions.
The present invention also relates to methods for producing a fermentation product, comprising:
(a) saccharifying a cellulosic material with an enzyme composition under anaerobic conditions;
(b) fermenting the saccharified cellulosic material with one or more fermenting microorganisms to produce the fermentation product; and
(c) recovering the fermentation product from the fermentation.
The present invention further relates to methods of fermenting a cellulosic material, comprising: fermenting the cellulosic material with one or more fermenting microorganisms, wherein the cellulosic material is hydrolyzed with an enzyme composition under anaerobic conditions.



BRIEF DESCRIPTION OF THE FIGURES
FIGS. 1A and 1B show reduced cellobiose dehydrogenase (CBDH) inhibition of pretreated corn stover (PCS) hydrolysis by a Trichoderma reesei cellulase composition under anaerobic conditions. Panel A: fractional cellulose conversion is plotted for various hydrolysis conditions. Solid bars: anaerobic hydrolysis; hatched bars: aerobic hydrolysis. Panel B: fractional cellulose conversion is plotted for cellobiose dehydrogenase inhibition of the Trichoderma reesei cellulase composition under anaerobic (open circles) and aerobic (closed circles) conditions.
FIG. 2 shows a comparison of aerobic and anaerobic hydrolysis of PCS at various concentrations of a Trichoderma reesei cellulase composition. Circles: 1 day hydrolysis; squares: 4 day hydrolysis; diamonds: 7 day hydrolysis; open symbols: anaerobic hydrolysis; closed symbols: aerobic hydrolysis.
FIG. 3 shows a comparison of aerobic and anaerobic hydrolysis of AVICEL® by a Trichoderma reesei cellulase composition, as well as ferrous iron inhibition of the Trichoderma reesei cellulase composition under aerobic and anaerobic hydrolysis conditions.



DEFINITIONS
Anaerobic conditions: The term “anaerobic conditions” is defined herein as processing conditions in the absence of molecular oxygen, or at an oxygen level significantly lower than those from ambient, atmospheric conditions (approximately 0.2 atmosphere pressure of oxygen gas or approximately 0.3 mM water-dissolved oxygen).
In one aspect, the oxygen level is preferably no greater than 0.15, more preferably no greater than 0.1, more preferably no greater than 0.05, more preferably no greater than 0.02, even more preferably no greater than 0.01, and most preferably no greater than 0.002 atmosphere pressure of oxygen gas. In another aspect, the oxygen level is preferably no greater than 0.15 atmosphere pressure of oxygen gas. In another aspect, the oxygen level is preferably no greater than 0.1 atmosphere pressure of oxygen gas. In another aspect, the oxygen level is preferably no greater than 0.05 atmosphere pressure of oxygen gas. In another aspect, the oxygen level is no greater than 0.02 atmosphere pressure of oxygen gas. In another aspect, the oxygen level is 0.01 atmosphere pressure of oxygen gas. In another aspect, the oxygen level is no greater than 0.002 atmosphere pressure of oxygen gas.
In another aspect, the oxygen level is preferably no greater than 0.25 mM, more preferably no greater than 0.2 mM, more preferably no greater than 0.15 mM, more preferably no greater than 0.1 mM, more preferably no greater than 0.05 mM, more preferably no greater than 0.025 mM, more preferably no greater than 0.01 mM, even more preferably no greater 0.002 mM, and most preferably no greater than 0.001 mM water-dissolved oxygen. In another aspect, the oxygen level is preferably no greater than 0.25 mM water-dissolved oxygen. In another aspect, the oxygen level is preferably no greater than 0.2 mM water-dissolved oxygen. In another aspect, the oxygen level is preferably no greater than 0.15 mM water-dissolved oxygen. In another aspect, the oxygen level is preferably no greater than 0.1 mM water-dissolved oxygen. In another aspect, the oxygen level is preferably no greater than 0.05 mM water-dissolved oxygen. In another aspect, the oxygen level is preferably no greater than 0.025 mM water-dissolved oxygen. In another aspect, the oxygen level is preferably no greater than 0.01 mM water-dissolved oxygen. In another aspect, the oxygen level is preferably no greater than 0.002 mM water-dissolved oxygen. In another aspect, the oxygen level is preferably no greater than 0.001 mM water-dissolved oxygen.
Cellobiose dehydrogenase: The term “cellobiose dehydrogenase” is defined herein as a cellobiose:acceptor 1-oxidoreductase (E.C. 1.1.99.18) that catalyzes the conversion of cellobiose in the presence of an acceptor to cellobiono-1,5-lactone and a reduced acceptor. 2,6-Dichlorophenolindophenol can act as acceptor, as can iron, especially Fe(SCN)3, molecular oxygen, ubiquinone, or cytochrome C, and likely many other polyphenolics. Substrates of the enzyme are cellobiose, cello-oligosaccharides, lactose, and D-glucosyl-1,4-β-D-mannose.
Cellobiose dehydrogenases comprise two families, 1 and 2, differentiated by the presence of a cellulose binding motif (CBM). The 3-dimensional structure of cellobiose dehydrogenase features two globular domains, each containing one of two cofactors: a heme or a flavin. The active site lies at a cleft between the two domains. The catalytic cycle of cellobiose dehydrogenase follows an ordered sequential mechanism. Oxidation of cellobiose occurs via 2-electron transfer from cellobiose to the flavin, generating cellobiono-1,5-lactone and reduced flavin. The active FAD is regenerated by electron transfer to the heme group, leaving a reduced heme. The native state heme is regenerated by reaction with the oxidizing substrate at the second active site.
The oxidizing substrate is preferentially iron ferricyanide, cytochrome C, or an oxidized phenolic compound such as dichloroindophenol (DCIP), a substrate commonly used for colorimetric assays. Metal ions and O2 are also substrates, but for most cellobiose dehydrogenases the reaction rate for these substrates is several orders of magnitude lower than that observed for iron or organic oxidants. Following cellobionolactone release, the product may undergo spontaneous ring-opening to generate cellobionic acid (Hallberg et al., 2003, J. Biol. Chem. 278: 7160-7166).
Cellulolytic activity: The term “cellulolytic activity” is defined herein as a biological activity that hydrolyzes a cellulosic material. The two basic approaches for measuring cellulolytic activity include: (1) measuring the total cellulolytic activity, and (2) measuring the individual cellulolytic activities (endoglucanases, cellobiohydrolases, and beta-glucosidases) as reviewed in Zhang et al., Outlook for cellulase improvement: Screening and selection strategies, 2006, Biotechnology Advances 24: 452-481. Total cellulolytic activity is usually measured using insoluble substrates, including Whatman No 1 filter paper, microcrystalline cellulose, bacterial cellulose, algal cellulose, cotton, pretreated lignocellulose, etc. The most common total cellulolytic activity assay is the filter paper assay using Whatman No 1 filter paper as the substrate. The assay was established by the International Union of Pure and Applied Chemistry (IUPAC) (chose, 1987, Measurement of cellulase activities, Pure Appl. Chem. 59: 257-68).
For purposes of the present invention, cellulolytic activity is determined by measuring the increase in hydrolysis of a cellulosic material by cellulolytic enzyme(s) under the following conditions: 1-20 mg of cellulolytic protein/g of cellulose in PCS for 3-7 days at 50-65° C. compared to a control hydrolysis without addition of cellulolytic protein. Typical conditions are 1 ml reactions, washed or unwashed PCS, 5% insoluble solids, 50 mM sodium acetate pH 5, 1 mM MnSO4, 50-65° C., 72 hours, sugar analysis by AMINEX® HPX-87H column (Bio-Rad Laboratories, Inc., Hercules, Calif., USA).
Endoglucanase: The term “endoglucanase” is defined herein as an endo-1,4-(1,3; 1,4)-beta-D-glucan 4-glucanohydrolase (E.C. 3.2.1.4), which catalyses endohydrolysis of 1,4-beta-D-glycosidic linkages in cellulose, cellulose derivatives (such as carboxymethyl cellulose and hydroxyethyl cellulose), lichenin, beta-1,4 bonds in mixed beta-1,3 glucans such as cereal beta-D-glucans or xyloglucans, and other plant material containing cellulosic components. Endoglucanase activity can be determined based on a reduction in substrate viscosity or increase in reducing ends determined by a reducing sugar assay (Zhang et al., 2006, Biotechnology Advances 24: 452-481). For purposes of the present invention, endoglucanase activity is determined using carboxymethyl cellulose (CMC) hydrolysis according to the procedure of Ghose, 1987, Pure and Appl. Chem. 59: 257-268.
Cellobiohydrolase: The term “cellobiohydrolase” is defined herein as a 1,4-beta-D-glucan cellobiohydrolase (E.C. 3.2.1.91), which catalyzes the hydrolysis of 1,4-beta-D-glucosidic linkages in cellulose, cellooligosaccharides, or any beta-1,4-linked glucose containing polymer, releasing cellobiose from the reducing or non-reducing ends of the chain (Teeri, 1997, Crystalline cellulose degradation: New insight into the function of cellobiohydrolases, Trends in Biotechnology 15: 160-167; Teeri et al., 1998, Trichoderma reesei cellobiohydrolases: why so efficient on crystalline cellulose?, Biochem. Soc. Trans. 26: 173-178). For purposes of the present invention, cellobiohydrolase activity is determined using a fluorescent disaccharide derivative 4-methylumbelliferyl-β-D-lactoside according to the procedures described by van Tilbeurgh et al., 1982, FEBS Letters 149: 152-156 and van Tilbeurgh and Claeyssens, 1985, FEBS Letters 187: 283-288.
Beta-glucosidase: The term “beta-glucosidase” is defined herein as a beta-D-glucoside glucohydrolase (E.C. 3.2.1.21), which catalyzes the hydrolysis of terminal non-reducing beta-D-glucose residues with the release of beta-D-glucose. For purposes of the present invention, beta-glucosidase activity is determined according to the basic procedure described by Venturi et al., 2002, Extracellular beta-D-glucosidase from Chaetomium thermophilum var. coprophilum: production, purification and some biochemical properties, J. Basic Microbiol. 42: 55-66. One unit of beta-glucosidase activity is defined as 1.0 μmole of p-nitrophenol produced per minute at 40° C., pH 5 from 1 mM p-nitrophenyl-beta-D-glucopyranoside as substrate in 100 mM sodium citrate containing 0.01% TWEEN® 20.
Cellulolytic enhancing activity: The term “cellulolytic enhancing activity” is defined herein as a biological activity that enhances the hydrolysis of a cellulosic material by polypeptides having cellulolytic activity. For purposes of the present invention, cellulolytic enhancing activity is determined by measuring the increase in reducing sugars or the increase of the total of cellobiose and glucose from the hydrolysis of a cellulosic material by cellulolytic protein under the following conditions: 1-50 mg of total protein/g of cellulose in PCS, wherein total protein is comprised of 50-99.5% w/w cellulolytic protein and 0.5-50% w/w protein of cellulolytic enhancing activity for 1-7 day at 50-65° C. compared to a control hydrolysis with equal total protein loading without cellulolytic enhancing activity (1-50 mg of cellulolytic protein/g of cellulose in PCS). In a preferred aspect, a mixture of CELLUCLAST® 1.5 L (Novozymes A/S, Bagsværd, Denmark) in the presence of 3% of total protein weight Aspergillus oryzae beta-glucosidase (recombinantly produced in Aspergillus oryzae according to WO 02/095014) or 3% of total protein weight Aspergillus fumigatus beta-glucosidase (recombinantly produced in Aspergillus oryzae as described in WO 2002/095014) of cellulase protein loading is used as the source of the cellulolytic activity.
The polypeptides having cellulolytic enhancing activity enhance the hydrolysis of a cellulosic material catalyzed by proteins having cellulolytic activity by reducing the amount of cellulolytic enzyme required to reach the same degree of hydrolysis preferably at least 1.01-fold, more preferably at least 1.05-fold, more preferably at least 1.10-fold, more preferably at least 1.25-fold, more preferably at least 1.5-fold, more preferably at least 2-fold, more preferably at least 3-fold, more preferably at least 4-fold, more preferably at least 5-fold, even more preferably at least 10-fold, and most preferably at least 20-fold.
Family 61 glycoside hydrolase: The term “Family 61 glycoside hydrolase” or “Family GH61” is defined herein as a polypeptide falling into the glycoside hydrolase Family 61 according to Henrissat B., 1991, A classification of glycosyl hydrolases based on amino-acid sequence similarities, Biochem. J. 280: 309-316, and Henrissat B., and Bairoch A., 1996, Updating the sequence-based classification of glycosyl hydrolases, Biochem. J. 316: 695-696. Presently, Henrissat lists the GH61 Family as unclassified indicating that properties such as mechanism, catalytic nucleophile/base, and catalytic proton donors are not known for polypeptides belonging to this family.
Xylan degrading activity: The terms “xylan degrading activity” or “xylanolytic activity” are defined herein as a biological activity that hydrolyzes xylan-containing material. The two basic approaches for measuring xylanolytic activity include: (1) measuring the total xylanolytic activity, and (2) measuring the individual xylanolytic activities (endoxylanases, beta-xylosidases, arabinofuranosidases, alpha-glucuronidases, acetylxylan esterases, feruloyl esterases, and alpha-glucuronyl esterases). Recent progress in assays of xylanolytic enzymes was summarized in several publications including Biely and Puchard, Recent progress in the assays of xylanolytic enzymes, 2006, Journal of the Science of Food and Agriculture 86(11): 1636-1647; Spanikova and Biely, 2006, Glucuronoyl esterase—Novel carbohydrate esterase produced by Schizophyllum commune, FEBS Letters 580(19): 4597-4601; Herrmann, Vrsanska, Jurickova, Hirsch, Biely, and Kubicek, 1997, The beta-D-xylosidase of Trichoderma reesei is a multifunctional beta-D-xylan xylohydrolase, Biochemical Journal 321: 375-381.
Total xylan degrading activity can be measured by determining the reducing sugars formed from various types of xylan, including oat spelt, beechwood, and larchwood xylans, or by photometric determination of dyed xylan fragments released from various covalently dyed xylans. The most common total xylanolytic activity assay is based on production of reducing sugars from polymeric 4-O-methyl glucuronoxylan as described in Bailey, Biely, Poutanen, 1992, Interlaboratory testing of methods for assay of xylanase activity, Journal of Biotechnology 23(3): 257-270.
For purposes of the present invention, xylan degrading activity is determined by measuring the increase in hydrolysis of birchwood xylan (Sigma Chemical Co., Inc., St. Louis, Mo., USA) by xylan-degrading enzyme(s) under the following typical conditions: 1 ml reactions, 5 mg/ml substrate (total solids), 5 mg of xylanolytic protein/g of substrate, 50 mM sodium acetate pH 5, 50° C., 24 hours, sugar analysis using p-hydroxybenzoic acid hydrazide (PHBAH) assay as described by Lever, 1972, A new reaction for colorimetric determination of carbohydrates, Anal. Biochem 47: 273-279.
Xylanase activity: The term “xylanase activity” is defined herein as a 1,4-beta-D-xylan-xylohydrolase activity (E.C. 3.2.1.8) that catalyzes the endo-hydrolysis of 1,4-beta-D-xylosidic linkages in xylans. For purposes of the present invention, xylanase activity is determined using birchwood xylan as substrate. One unit of xylanase activity is defined as 1.0 μmole of reducing sugar (measured in glucose equivalents as described by Lever, 1972, A new reaction for colorimetric determination of carbohydrates, Anal. Biochem 47: 273-279) produced per minute during the initial period of hydrolysis at 50° C., pH 5 from 2 g of birchwood xylan per liter as substrate in 50 mM sodium acetate containing 0.01% TWEEN® 20.
Beta-xylosidase activity: The term “beta-xylosidase activity” is defined herein as a beta-D-xyloside xylohydrolase (E.C. 3.2.1.37) that catalyzes the exo-hydrolysis of short beta (1→4)-xylooligosaccharides, to remove successive D-xylose residues from the non-reducing termini. For purposes of the present invention, one unit of beta-xylosidase activity is defined as 1.0 μmole of p-nitrophenol produced per minute at 40° C., pH 5 from 1 mM p-nitrophenyl-beta-D-xyloside as substrate in 100 mM sodium citrate containing 0.01% TWEEN® 20.
Acetylxylan esterase activity: The term “acetylxylan esterase activity” is defined herein as a carboxylesterase activity (EC 3.1.1.72) that catalyses the hydrolysis of acetyl groups from polymeric xylan, acetylated xylose, acetylated glucose, alpha-napthyl acetate, and p-nitrophenyl acetate. For purposes of the present invention, acetylxylan esterase activity is determined using 0.5 mM p-nitrophenylacetate as substrate in 50 mM sodium acetate pH 5.0 containing 0.01% TWEENTM 20. One unit of acetylxylan esterase activity is defined as the amount of enzyme capable of releasing 1 μmole of p-nitrophenolate anion per minute at pH 5, 25° C.
Feruloyl esterase activity: The term “feruloyl esterase activity” is defined herein as a 4-hydroxy-3-methoxycinnamoyl-sugar hydrolase activity (EC 3.1.1.73) that catalyzes the hydrolysis of the 4-hydroxy-3-methoxycinnamoyl (feruloyl) group from an esterified sugar, which is usually arabinose in “natural” substrates, to produce ferulate (4-hydroxy-3-methoxycinnamate). Feruloyl esterase is also known as ferulic acid esterase, hydroxycinnamoyl esterase, FAE-III, cinnamoyl ester hydrolase, FAEA, cinnAE, FAE-I, or FAE-II. For purposes of the present invention, feruloyl esterase activity is determined using 0.5 mM p-nitrophenylferulate as substrate in 50 mM sodium acetate pH 5.0. One unit of feruloyl esterase activity equals the amount of enzyme capable of releasing 1 μmole of p-nitrophenolate anion per minute at pH 5, 25° C.
Alpha-glucuronidase activity: The term “alpha-glucuronidase activity” is defined herein as an alpha-D-glucosiduronate glucuronohydrolase activity (EC 3.2.1.139) that catalyzes the hydrolysis of an alpha-D-glucuronoside to D-glucuronate and an alcohol. For purposes of the present invention, alpha-glucuronidase activity is determined according to de Vries, 1998, J. Bacteriol. 180: 243-249. One unit of alpha-glucuronidase activity equals the amount of enzyme capable of releasing 1 μmole of glucuronic or 4-O-methylglucuronic acid per minute at pH 5, 40° C.
Alpha-L-arabinofuranosidase activity: The term “alpha-L-arabinofuranosidase activity” is defined herein as an alpha-L-arabinofuranoside arabinofuranohydrolase activity (EC 3.2.1.55) that catalyzes the hydrolysis of terminal non-reducing alpha-L-arabinofuranoside residues in alpha-L-arabinosides. The enzyme activity acts on alpha-L-arabinofuranosides, alpha-L-arabinans containing (1,3)- and/or (1,5)-linkages, arabinoxylans, and arabinogalactans. Alpha-L-arabinofuranosidase is also known as arabinosidase, alpha-arabinosidase, alpha-L-arabinosidase, alpha-arabinofuranosidase, polysaccharide alpha-L-arabinofuranosidase, alpha-L-arabinofuranoside hydrolase, L-arabinosidase, or alpha-L-arabinanase. For purposes of the present invention, alpha-L-arabinofuranosidase activity is determined using 5 mg of medium viscosity wheat arabinoxylan (Megazyme International Ireland, Ltd., Bray, Co. Wicklow, Ireland) per ml of 100 mM sodium acetate pH 5 in a total volume of 200 μl for 30 minutes at 40° C. followed by arabinose analysis by AMINEX® HPX-87H column chromatography (Bio-Rad Laboratories, Inc., Hercules, Calif., USA).
Cellulosic material: The cellulosic material can be any material containing cellulose. The predominant polysaccharide in the primary cell wall of biomass is cellulose, the second most abundant is hemicellulose, and the third is pectin. The secondary cell wall, produced after the cell has stopped growing, also contains polysaccharides and is strengthened by polymeric lignin covalently cross-linked to hemicellulose. Cellulose is a homopolymer of anhydrocellobiose and thus a linear beta-(1-4)-D-glucan, while hemicelluloses include a variety of compounds, such as xylans, xyloglucans, arabinoxylans, and mannans in complex branched structures with a spectrum of substituents. Although generally polymorphous, cellulose is found in plant tissue primarily as an insoluble crystalline matrix of parallel glucan chains. Hemicelluloses usually hydrogen bond to cellulose, as well as to other hemicelluloses, which help stabilize the cell wall matrix.
Cellulose is generally found, for example, in the stems, leaves, hulls, husks, and cobs of plants or leaves, branches, and wood of trees. The cellulosic material can be, but is not limited to, herbaceous material, agricultural residue, forestry residue, municipal solid waste, waste paper, and pulp and paper mill residue (see, for example, Wiselogel et al., 1995, in Handbook on Bioethanol (Charles E. Wyman, editor), pp. 105-118, Taylor & Francis, Washington D.C.; Wyman, 1994, Bioresource Technology 50: 3-16; Lynd, 1990, Applied Biochemistry and Biotechnology 24/25: 695-719; Mosier et al., 1999, Recent Progress in Bioconversion of Lignocellulosics, in Advances in Biochemical Engineering/Biotechnology, T. Scheper, managing editor, Volume 65, pp. 23-40, Springer-Verlag, New York). It is understood herein that the cellulose may be in the form of lignocellulose, a plant cell wall material containing lignin, cellulose, and hemicellulose in a mixed matrix. In a preferred aspect, the cellulosic material is lignocellulose.
In one aspect, the cellulosic material is herbaceous material. In another aspect, the cellulosic material is agricultural residue. In another aspect, the cellulosic material is forestry residue. In another aspect, the cellulosic material is municipal solid waste. In another aspect, the cellulosic material is waste paper. In another aspect, the cellulosic material is pulp and paper mill residue.
In another aspect, the cellulosic material is corn stover. In another aspect, the cellulosic material is corn fiber. In another aspect, the cellulosic material is corn cob. In another aspect, the cellulosic material is orange peel. In another aspect, the cellulosic material is rice straw. In another aspect, the cellulosic material is wheat straw. In another aspect, the cellulosic material is switch grass. In another aspect, the cellulosic material is miscanthus. In another aspect, the cellulosic material is bagasse.
In another aspect, the cellulosic material is microcrystalline cellulose. In another aspect, the cellulosic material is bacterial cellulose. In another aspect, the cellulosic material is algal cellulose. In another aspect, the cellulosic material is cotton linter. In another aspect, the cellulosic material is amorphous phosphoric-acid treated cellulose. In another aspect, the cellulosic material is filter paper.
The cellulosic material may be used as is or may be subjected to pretreatment, using conventional methods known in the art, as described herein. In a preferred aspect, the cellulosic material is pretreated.
Pretreated corn stover: The term “PCS” or “Pretreated Corn Stover” is defined herein as a cellulosic material derived from corn stover by treatment with heat and dilute sulfuric acid.
Xylan-containing material: The term “xylan-containing material” is defined herein as any material comprising a plant cell wall polysaccharide containing a backbone of beta-(1-4)-linked xylose residues. Xylans of terrestrial plants are heteropolymers possessing a beta-(1-4)-D-xylopyranose backbone, which is branched by short carbohydrate chains. They comprise D-glucuronic acid or its 4-O-methyl ether, L-arabinose, and/or various oligosaccharides, composed of D-xylose, L-arabinose, D- or L-galactose, and D-glucose. Xylan-type polysaccharides can be divided into homoxylans and heteroxylans, which include glucuronoxylans, (arabino)glucuronoxylans, (glucurono)arabinoxylans, arabinoxylans, and complex heteroxylans. See, for example, Ebringerova et al., 2005, Adv. Polym. Sci. 186: 1-67.
In the methods of the present invention, any material containing xylan may be used. In a preferred aspect, the xylan-containing material is lignocellulose.
Isolated polypeptide: The term “isolated polypeptide” as used herein refers to a polypeptide that is isolated from a source. In a preferred aspect, the polypeptide is at least 1% pure, preferably at least 5% pure, more preferably at least 10% pure, more preferably at least 20% pure, more preferably at least 40% pure, more preferably at least 60% pure, even more preferably at least 80% pure, and most preferably at least 90% pure, as determined by SDS-PAGE.
Substantially pure polypeptide: The term “substantially pure polypeptide” denotes herein a polypeptide preparation that contains at most 10%, preferably at most 8%, more preferably at most 6%, more preferably at most 5%, more preferably at most 4%, more preferably at most 3%, even more preferably at most 2%, most preferably at most 1%, and even most preferably at most 0.5% by weight of other polypeptide material with which it is natively or recombinantly associated. It is, therefore, preferred that the substantially pure polypeptide is at least 92% pure, preferably at least 94% pure, more preferably at least 95% pure, more preferably at least 96% pure, more preferably at least 97% pure, more preferably at least 98% pure, even more preferably at least 99% pure, most preferably at least 99.5% pure, and even most preferably 100% pure by weight of the total polypeptide material present in the preparation. The polypeptides are preferably in a substantially pure form, i.e., that the polypeptide preparation is essentially free of other polypeptide material with which it is natively or recombinantly associated. This can be accomplished, for example, by preparing the polypeptide by well-known recombinant methods or by classical purification methods.
Mature polypeptide: The term “mature polypeptide” is defined herein as a polypeptide in its final form following translation and any post-translational modifications, such as N-terminal processing, C-terminal truncation, glycosylation, phosphorylation, etc.
Mature polypeptide coding sequence: The term “mature polypeptide coding sequence” is defined herein as a nucleotide sequence that encodes a mature polypeptide.
Identity: The relatedness between two amino acid sequences or between two nucleotide sequences is described by the parameter “identity”.
For purposes of the present invention, the degree of identity between two amino acid sequences is determined using the Needleman-Wunsch algorithm (Needleman and Wunsch, 1970, J. Mol. Biol. 48: 443-453) as implemented in the Needle program of the EMBOSS package (EMBOSS: The European Molecular Biology Open Software Suite, Rice et al., 2000, Trends in Genetics 16: 276-277), preferably version 3.0.0 or later. The optional parameters used are gap open penalty of 10, gap extension penalty of 0.5, and the EBLOSUM62 (EMBOSS version of BLOSUM62) substitution matrix. The output of Needle labeled “longest identity” (obtained using the—nobrief option) is used as the percent identity and is calculated as follows:

(Identical Residues×100)/(Length of Alignment−Total Number of Gaps in Alignment)

For purposes of the present invention, the degree of identity between two deoxyribonucleotide sequences is determined using the Needleman-Wunsch algorithm (Needleman and Wunsch, 1970, supra) as implemented in the Needle program of the EMBOSS package (EMBOSS: The European Molecular Biology Open Software Suite, Rice et al., 2000, supra), preferably version 3.0.0 or later. The optional parameters used are gap open penalty of 10, gap extension penalty of 0.5, and the EDNAFULL (EMBOSS version of NCBI NUC4.4) substitution matrix. The output of Needle labeled “longest identity” (obtained using the—nobrief option) is used as the percent identity and is calculated as follows:

(Identical Deoxyribonucleotides×100)/(Length of Alignment−Total Number of Gaps in Alignment)

Homologous sequence: The term “homologous sequence” is defined herein as a predicted protein having an E value (or expectancy score) of less than 0.001 in a tfasty search (Pearson, W. R., 1999, in Bioinformatics Methods and Protocols, S. Misener and S. A. Krawetz, ed., pp. 185-219) with a polypeptide of interest.
Polypeptide fragment: The term “polypeptide fragment” is defined herein as a polypeptide having one or more (several) amino acids deleted from the amino and/or carboxyl terminus of a mature polypeptide or a homologous sequence thereof.
Subsequence: The term “subsequence” is defined herein as a nucleotide sequence having one or more (several) nucleotides deleted from the 5′ and/or 3′ end of a mature polypeptide coding sequence or a homologous sequence thereof.
Allelic variant: The term “allelic variant” denotes herein any of two or more alternative forms of a gene occupying the same chromosomal locus. Allelic variation arises naturally through mutation, and may result in polymorphism within populations. Gene mutations can be silent (no change in the encoded polypeptide) or may encode polypeptides having altered amino acid sequences. An allelic variant of a polypeptide is a polypeptide encoded by an allelic variant of a gene.
Isolated polynucleotide: The term “isolated polynucleotide” as used herein refers to a polynucleotide that is isolated from a source. In a preferred aspect, the polynucleotide is at least 1% pure, preferably at least 5% pure, more preferably at least 10% pure, more preferably at least 20% pure, more preferably at least 40% pure, more preferably at least 60% pure, even more preferably at least 80% pure, and most preferably at least 90% pure, as determined by agarose electrophoresis.
Substantially pure polynucleotide: The term “substantially pure polynucleotide” as used herein refers to a polynucleotide preparation free of other extraneous or unwanted nucleotides and in a form suitable for use within genetically engineered protein production systems. Thus, a substantially pure polynucleotide contains at most 10%, preferably at most 8%, more preferably at most 6%, more preferably at most 5%, more preferably at most 4%, more preferably at most 3%, even more preferably at most 2%, most preferably at most 1%, and even most preferably at most 0.5% by weight of other polynucleotide material with which it is natively or recombinantly associated. A substantially pure polynucleotide may, however, include naturally occurring 5′ and 3′ untranslated regions, such as promoters and terminators. It is preferred that the substantially pure polynucleotide is at least 90% pure, preferably at least 92% pure, more preferably at least 94% pure, more preferably at least 95% pure, more preferably at least 96% pure, more preferably at least 97% pure, even more preferably at least 98% pure, most preferably at least 99% pure, and even most preferably at least 99.5% pure by weight. The polynucleotides are preferably in a substantially pure form, i.e., that the polynucleotide preparation is essentially free of other polynucleotide material with which it is natively or recombinantly associated. The polynucleotides may be of genomic, cDNA, RNA, semisynthetic, synthetic origin, or any combinations thereof.
Coding sequence: When used herein the term “coding sequence” means a nucleotide sequence, which directly specifies the amino acid sequence of its protein product. The boundaries of the coding sequence are generally determined by an open reading frame, which usually begins with the ATG start codon or alternative start codons such as GTG and TTG and ends with a stop codon such as TAA, TAG, and TGA. The coding sequence may be a DNA, cDNA, synthetic, or recombinant nucleotide sequence.
cDNA: The term “cDNA” is defined herein as a DNA molecule that can be prepared by reverse transcription from a mature, spliced, mRNA molecule obtained from a eukaryotic cell. cDNA lacks intron sequences that may be present in the corresponding genomic DNA. The initial, primary RNA transcript is a precursor to mRNA that is processed through a series of steps before appearing as mature spliced mRNA. These steps include the removal of intron sequences by a process called splicing. cDNA derived from mRNA lacks, therefore, any intron sequences.
Nucleic acid construct: The term “nucleic acid construct” as used herein refers to a nucleic acid molecule, either single- or double-stranded, which is isolated from a naturally occurring gene or which is modified to contain segments of nucleic acids in a manner that would not otherwise exist in nature or which is synthetic. The term nucleic acid construct is synonymous with the term “expression cassette” when the nucleic acid construct contains the control sequences required for expression of a coding sequence.
Control sequences: The term “control sequences” is defined herein to include all components necessary for the expression of a polynucleotide encoding a polypeptide. Each control sequence may be native or foreign to the nucleotide sequence encoding the polypeptide or native or foreign to each other. Such control sequences include, but are not limited to, a leader, polyadenylation sequence, propeptide sequence, promoter, signal peptide sequence, and transcription terminator. At a minimum, the control sequences include a promoter, and transcriptional and translational stop signals. The control sequences may be provided with linkers for the purpose of introducing specific restriction sites facilitating ligation of the control sequences with the coding region of the nucleotide sequence encoding a polypeptide.
Operably linked: The term “operably linked” denotes herein a configuration in which a control sequence is placed at an appropriate position relative to the coding sequence of the polynucleotide sequence such that the control sequence directs the expression of the coding sequence of a polypeptide.
Expression: The term “expression” includes any step involved in the production of a polypeptide including, but not limited to, transcription, post-transcriptional modification, translation, post-translational modification, and secretion.
Expression vector: The term “expression vector” is defined herein as a linear or circular DNA molecule that comprises a polynucleotide encoding a polypeptide and is operably linked to additional nucleotides that provide for its expression.
Host cell: The term “host cell”, as used herein, includes any cell type that is susceptible to transformation, transfection, transduction, and the like with a nucleic acid construct or expression vector comprising a polynucleotide of the present invention.
Modification: The term “modification” means herein any chemical modification of a polypeptide, as well as genetic manipulation of the DNA encoding the polypeptide. The modification can be a substitution, a deletion and/or an insertion of one or more (several) amino acids as well as replacements of one or more (several) amino acid side chains.
Artificial variant: When used herein, the term “artificial variant” means a polypeptide produced by an organism expressing a modified polynucleotide sequence encoding a polypeptide variant. The modified nucleotide sequence is obtained through human intervention by modification of the polynucleotide sequence.
DETAILED DESCRIPTION OF THE INVENTION
The present invention relates to methods for pretreating a cellulosic material, comprising: pretreating the cellulosic material under anaerobic conditions. In one aspect, the method further comprises recovering the pretreated cellulosic material.
The present invention also relates to methods for degrading or converting a cellulosic material, comprising: treating the cellulosic material with an enzyme composition under anaerobic conditions. In one aspect, the method further comprises recovering the degraded or converted cellulosic material.
The present invention also relates to methods for producing a fermentation product, comprising: (a) saccharifying a cellulosic material with an enzyme composition under anaerobic conditions; (b) fermenting the saccharified cellulosic material with one or more fermenting microorganisms to produce the fermentation product; and (c) recovering the fermentation product from the fermentation.
The present invention further relates to methods of fermenting a cellulosic material, comprising: fermenting the cellulosic material with one or more fermenting microorganisms, wherein the cellulosic material is saccharified with an enzyme composition under anaerobic conditions. In one aspect, the fermenting of the cellulosic material produces a fermentation product. In another aspect, the method further comprises recovering the fermentation product from the fermentation.
In the methods described above, pretreating or hydrolyzing the cellulosic material under anaerobic conditions improves the extent and/or rate of hydrolysis or conversion of cellulose to soluble, fermentable sugars by a cellulolytic enzyme composition.
In practicing the methods of the present invention, any anaerobic system known in the art can be used. Anaerobic reactors are widely used in various industries, including wastewater treatment, industrial/municipal waste digester, and biogas generation (see, for example, Castro-Gonzalez, A., Enriquez, M., Dura, C., 2001, Design, construction, and starting-up of an anaerobic reactor for the stabilisation, handling, and disposal of excess biological sludge generated in a wastewater treatment plant, Anaerobe 7: 143-149; Melidis, P., Georgiou, D., Aivasidis, A., 2003, Scale-up and design optimization of anaerobic immobilized cell reactors for wastewater treatment, Chemical Engineering and Processing 42: 897-908). In general, the system may include, but is not limited to, one or more valved inlets to feed biomass feedstock, pretreatment agents (e.g., acid), inert (non-oxygen) gas, water, post-pretreatment agents (e.g., acid-neutralizing base), etc., one or more valved outlets to dispense pretreated biomass, spent liquor, reacted/generated gas, etc., one or more mechanical stirring devices for mixing, one or more monitors for pH, volume, gas, and temperature control, assembled in an enclosed assembly in which any contact with atmospheric oxygen is controlled/limited.
Anaerobicity may be achieved by air limitation, O2 sequestration, bubbling/blanketing with an inert gas such as N2, CO2, Ar, etc., or a combination thereof. One preferred method is to fully fill a reactor with degassed biomass suspension liquor with no/minimal head space. Another preferred way is to bubble and blanket a biomass hydrolysis suspension with CO2, collected and delivered from a sugar-to-ethanol fermentation reactor where the gas is a by-product. CO2 collection is used in several industries, such as beer manufacturing (for reference, see for example, Redford, S G (1997) Multi-stage column continuous fermentation system, U.S. Pat. No. 5,925,563; Coors Shenandoah: Peak Performance, Beverage World, Jun. 15, 2008). A generic procedure can, but is not limited to, comprise a gas outlet mounted at the top of a sugar-to-ethanol fermentor (to collect CO2), an enclosed pipe (to transport CO2) with or without a pressurizing pump, and an injection/feeding inlet mounted to a biomass hydrolysis reactor (to feed CO2).
The enzyme composition can be in the form of a crude fermentation broth with or without the cells removed or in the form of a semi-purified or purified enzyme preparation or the composition can comprise a host cell as a source of the enzyme composition in a fermentation process with the biomass.
The methods of the present invention can be used to saccharify a cellulosic material to fermentable sugars and convert the fermentable sugars to many useful substances, e.g., chemicals and fuels. The production of a desired fermentation product from cellulosic material typically involves pretreatment, enzymatic hydrolysis (saccharification), and fermentation.
The treatment of cellulosic material according to the present invention can be accomplished using processes conventional in the art. Moreover, the methods of the present invention can be implemented using any conventional biomass processing apparatus configured to operate in accordance with the invention.
Hydrolysis (saccharification) and fermentation, separate or simultaneous, include, but are not limited to, separate hydrolysis and fermentation (SHF); simultaneous saccharification and fermentation (SSF); simultaneous saccharification and cofermentation (SSCF); hybrid hydrolysis and fermentation (HHF); SHCF (separate hydrolysis and co-fermentation), HHCF (hybrid hydrolysis and fermentation), and direct microbial conversion (DMC). SHF uses separate process steps to first enzymatically hydrolyze lignocellulose to fermentable sugars, e.g., glucose, cellobiose, cellotriose, and pentose sugars, and then ferment the fermentable sugars to ethanol. In SSF, the enzymatic hydrolysis of lignocellulose and the fermentation of sugars to ethanol are combined in one step (Philippidis, G. P., 1996, Cellulose bioconversion technology, in Handbook on Bioethanol: Production and Utilization, Wyman, C. E., ed., Taylor & Francis, Washington, D.C., 179-212). SSCF involves the cofermentation of multiple sugars (Sheehan, J., and Himmel, M., 1999, Enzymes, energy and the environment: A strategic perspective on the U.S. Department of Energy's research and development activities for bioethanol, Biotechnol. Prog. 15: 817-827). HHF involves a separate hydrolysis separate step, and in addition a simultaneous saccharification and hydrolysis step, which can be carried out in the same reactor. The steps in an HHF process can be carried out at different temperatures, i.e., high temperature enzymatic saccharification followed by SSF at a lower temperature that the fermentation strain can tolerate. DMC combines all three processes (enzyme production, lignocellulose hydrolysis, and fermentation) in one or more steps where the same organism is used to produce the enzymes for conversion of the lignocellulose to fermentable sugars and to convert the fermentable sugars into a final product (Lynd, L. R., Weimer, P. J., van Zyl, W. H., and Pretorius, I. S., 2002, Microbial cellulose utilization: Fundamentals and biotechnology, Microbiol. Mol. Biol. Reviews 66: 506-577). It is understood herein that any method known in the art comprising pretreatment, enzymatic hydrolysis (saccharification), fermentation, or a combination thereof can be used in the practicing the methods of the present invention.
A conventional apparatus can include a fed-batch stirred reactor, a batch stirred reactor, a continuous flow stirred reactor with ultrafiltration, and/or a continuous plug-flow column reactor (Fernanda de Castilhos Corazza, Flávio Faria de Moraes, Gisella Maria Zanin and Ivo Neitzel, 2003, Optimal control in fed-batch reactor for the cellobiose hydrolysis, Acta Scientiarum. Technology 25: 33-38; Gusakov, A. V., and Sinitsyn, A. P., 1985, Kinetics of the enzymatic hydrolysis of cellulose: 1. A mathematical model for a batch reactor process, Enz. Microb. Technol. 7: 346-352), an attrition reactor (Ryu, S. K., and Lee, J. M., 1983, Bioconversion of waste cellulose by using an attrition bioreactor, Biotechnol. Bioeng. 25: 53-65), or a reactor with intensive stirring induced by an electromagnetic field (Gusakov, A. V., Sinitsyn, A. P., Davydkin, I. Y., Davydkin, V. Y., Protas, O. V., 1996, Enhancement of enzymatic cellulose hydrolysis using a novel type of bioreactor with intensive stirring induced by electromagnetic field, Appl. Biochem. Biotechnol. 56: 141-153). Additional reactor types include: Fluidized bed, upflow blanket, immobilized, and extruder type reactors for hydrolysis and/or fermentation.
Pretreatment. In practicing the methods of the present invention, any pretreatment process known in the art can be used to disrupt plant cell wall components of cellulosic material (Chandra et al., 2007, Substrate pretreatment: The key to effective enzymatic hydrolysis of lignocellulosics? Adv. Biochem. Engin./Biotechnol. 108: 67-93; Galbe and Zacchi, 2007, Pretreatment of lignocellulosic materials for efficient bioethanol production, Adv. Biochem. Engin./Biotechnol. 108: 41-65; Hendriks and Zeeman, 2009, Pretreatments to enhance the digestibility of lignocellulosic biomass, Bioresource Technol. 100: 10-18; Mosier et al., 2005, Features of promising technologies for pretreatment of lignocellulosic biomass, Bioresource Technol. 96: 673-686; Taherzadeh and Karimi, 2008, Pretreatment of lignocellulosic wastes to improve ethanol and biogas production: A review, Int. J. of Mol. Sci. 9: 1621-1651; Yang and Wyman, 2008, Pretreatment: the key to unlocking low-cost cellulosic ethanol, Biofuels Bioproducts and Biorefining-Biofpr. 2: 26-40).
The cellulosic material can also be subjected to particle size reduction, pre-soaking, wetting, washing, or conditioning prior to pretreatment using methods known in the art.
Conventional pretreatments include, but are not limited to, steam pretreatment (with or without explosion), dilute acid pretreatment, hot water pretreatment, alkaline pretreatment, lime pretreatment, wet oxidation, wet explosion, ammonia fiber explosion, organosolv pretreatment, and biological pretreatment. Additional pretreatments include ammonia percolation, ultrasound, electroporation, microwave, supercritical CO2, supercritical H2O, ozone, and gamma irradiation pretreatments.
The cellulosic material can be pretreated before hydrolysis and/or fermentation. Pretreatment is preferably performed prior to the hydrolysis. Alternatively, the pretreatment can be carried out simultaneously with enzyme hydrolysis to release fermentable sugars, such as glucose, xylose, and/or cellobiose. In most cases the pretreatment step itself results in some conversion of biomass to fermentable sugars (even in absence of enzymes).
Steam Pretreatment. In steam pretreatment, cellulosic material is heated to disrupt the plant cell wall components, including lignin, hemicellulose, and cellulose to make the cellulose and other fractions, e.g., hemicellulose, accessible to enzymes. Cellulosic material is passed to or through a reaction vessel where steam is injected to increase the temperature to the required temperature and pressure and is retained therein for the desired reaction time. Steam pretreatment is preferably done at 140-230° C., more preferably 160-200° C., and most preferably 170-190° C., where the optimal temperature range depends on any addition of a chemical catalyst. Residence time for the steam pretreatment is preferably 1-15 minutes, more preferably 3-12 minutes, and most preferably 4-10 minutes, where the optimal residence time depends on temperature range and any addition of a chemical catalyst. Steam pretreatment allows for relatively high solids loadings, so that cellulosic material is generally only moist during the pretreatment. The steam pretreatment is often combined with an explosive discharge of the material after the pretreatment, which is known as steam explosion, that is, rapid flashing to atmospheric pressure and turbulent flow of the material to increase the accessible surface area by fragmentation (Duff and Murray, 1996, Bioresource Technology 855: 1-33; Galbe and Zacchi, 2002, Appl. Microbiol. Biotechnol. 59: 618-628; U.S. Patent Application No. 20020164730). During steam pretreatment, hemicellulose acetyl groups are cleaved and the resulting acid autocatalyzes partial hydrolysis of the hemicellulose to monosaccharides and oligosaccharides. Lignin is removed to only a limited extent.
A catalyst such as H2SO4 or SO2 (typically 0.3 to 3% w/w) is often added prior to steam pretreatment, which decreases the time and temperature, increases the recovery, and improves enzymatic hydrolysis (Ballesteros et al., 2006, Appl. Biochem. Biotechnol. 129-132: 496-508; Varga et al., 2004, Appl. Biochem. Biotechnol. 113-116: 509-523; Sassner et al., 2006, Enzyme Microb. Technol. 39: 756-762).
Chemical Pretreatment: The term “chemical treatment” refers to any chemical pretreatment that promotes the separation and/or release of cellulose, hemicellulose, and/or lignin. Examples of suitable chemical pretreatment processes include, for example, dilute acid pretreatment, lime pretreatment, wet oxidation, ammonia fiber/freeze explosion (AFEX), ammonia percolation (APR), and organosolv pretreatments.
In dilute acid pretreatment, cellulosic material is mixed with dilute acid, typically H2SO4, and water to form a slurry, heated by steam to the desired temperature, and after a residence time flashed to atmospheric pressure. The dilute acid pretreatment can be performed with a number of reactor designs, e.g., plug-flow reactors, counter-current reactors, or continuous counter-current shrinking bed reactors (Duff and Murray, 1996, supra; Schell et al., 2004, Bioresource Technol. 91: 179-188; Lee et al., 1999, Adv. Biochem. Eng. Biotechnol. 65: 93-115).
Several methods of pretreatment under alkaline conditions can also be used. These alkaline pretreatments include, but are not limited to, lime pretreatment, wet oxidation, ammonia percolation (APR), and ammonia fiber/freeze explosion (AFEX).
Lime pretreatment is performed with calcium carbonate, sodium hydroxide, or ammonia at low temperatures of 85-150° C. and residence times from 1 hour to several days (Wyman et al., 2005, Bioresource Technol. 96: 1959-1966; Mosier et al., 2005, Bioresource Technol. 96: 673-686). WO 2006/110891, WO 2006/11899, WO 2006/11900, and WO 2006/110901 disclose pretreatment methods using ammonia.
Wet oxidation is a thermal pretreatment performed typically at 180-200° C. for 5-15 minutes with addition of an oxidative agent such as hydrogen peroxide or over-pressure of oxygen (Schmidt and Thomsen, 1998, Bioresource Technol. 64: 139-151; Palonen et al., 2004, Appl. Biochem. Biotechnol. 117: 1-17; Varga et al., 2004, Biotechnol. Bioeng. 88: 567-574; Martin et al., 2006, J. Chem. Technol. Biotechnol. 81: 1669-1677). The pretreatment is performed at preferably 1-40% dry matter, more preferably 2-30% dry matter, and most preferably 5-20% dry matter, and often the initial pH is increased by the addition of alkali such as sodium carbonate.
A modification of the wet oxidation pretreatment method, known as wet explosion (combination of wet oxidation and steam explosion), can handle dry matter up to 30%. In wet explosion, the oxidizing agent is introduced during pretreatment after a certain residence time. The pretreatment is then ended by flashing to atmospheric pressure (WO 2006/032282).
Ammonia fiber explosion (AFEX) involves treating cellulosic material with liquid or gaseous ammonia at moderate temperatures such as 90-100° C. and high pressure such as 17-20 bar for 5-10 minutes, where the dry matter content can be as high as 60% (Gollapalli et al., 2002, Appl. Biochem. Biotechnol. 98: 23-35; Chundawat et al., 2007, Biotechnol. Bioeng. 96: 219-231; Alizadeh et al., 2005, Appl. Biochem. Biotechnol. 121: 1133-1141; Teymouri et al., 2005, Bioresource Technol. 96: 2014-2018). AFEX pretreatment results in the depolymerization of cellulose and partial hydrolysis of hemicellulose. Lignin-carbohydrate complexes are cleaved.
Organosolv pretreatment delignifies cellulosic material by extraction using aqueous ethanol (40-60% ethanol) at 160-200° C. for 30-60 minutes (Pan et al., 2005, Biotechnol. Bioeng. 90: 473-481; Pan et al., 2006, Biotechnol. Bioeng. 94: 851-861; Kurabi et al., 2005, Appl. Biochem. Biotechnol. 121: 219-230). Sulphuric acid is usually added as a catalyst. In organosolv pretreatment, the majority of hemicellulose is removed.
Other examples of suitable pretreatment methods are described by Schell et al., 2003, Appl. Biochem. and Biotechnol. Vol. 105-108, p. 69-85, and Mosier et al., 2005, Bioresource Technology 96: 673-686, and U.S. Published Application 2002/0164730.
In one aspect, the chemical pretreatment is preferably carried out as an acid treatment, and more preferably as a continuous dilute and/or mild acid treatment. The acid is typically sulfuric acid, but other acids can also be used, such as acetic acid, citric acid, nitric acid, phosphoric acid, tartaric acid, succinic acid, hydrogen chloride, or mixtures thereof. Mild acid treatment is conducted in the pH range of preferably 1-5, more preferably 1-4, and most preferably 1-3. In one aspect, the acid concentration is in the range from preferably 0.01 to 20 wt % acid, more preferably 0.05 to 10 wt % acid, even more preferably 0.1 to 5 wt % acid, and most preferably 0.2 to 2.0 wt % acid. The acid is contacted with cellulosic material and held at a temperature in the range of preferably 160-220° C., and more preferably 165-195° C., for periods ranging from seconds to minutes to, e.g., 1 second to 60 minutes.
In another aspect, pretreatment is carried out as an ammonia fiber explosion step (AFEX pretreatment step).
In another aspect, pretreatment takes place in an aqueous slurry. In preferred aspects, cellulosic material is present during pretreatment in amounts preferably between 10-80 wt %, more preferably between 20-70 wt %, and most preferably between 30-60 wt %, such as around 50 wt %. The pretreated cellulosic material can be unwashed or washed using any method known in the art, e.g., washed with water.
Mechanical Pretreatment: The term “mechanical pretreatment” refers to various types of grinding or milling (e.g., dry milling, wet milling, or vibratory ball milling).
Physical Pretreatment: The term “physical pretreatment” refers to any pretreatment that promotes the separation and/or release of cellulose, hemicellulose, and/or lignin from cellulosic material. For example, physical pretreatment can involve irradiation (e.g., microwave irradiation), steaming/steam explosion, hydrothermolysis, and combinations thereof.
Physical pretreatment can involve high pressure and/or high temperature (steam explosion). In one aspect, high pressure means pressure in the range of preferably about 300 to about 600 psi, more preferably about 350 to about 550 psi, and most preferably about 400 to about 500 psi, such as around 450 psi. In another aspect, high temperature means temperatures in the range of about 100 to about 300° C., preferably about 140 to about 235° C. In a preferred aspect, mechanical pretreatment is performed in a batch-process, steam gun hydrolyzer system that uses high pressure and high temperature as defined above, e.g., a Sunds Hydrolyzer available from Sunds Defibrator AB, Sweden.
Combined Physical and Chemical Pretreatment: Cellulosic material can be pretreated both physically and chemically. For instance, the pretreatment step can involve dilute or mild acid treatment and high temperature and/or pressure treatment. The physical and chemical pretreatments can be carried out sequentially or simultaneously, as desired. A mechanical pretreatment can also be included.
Accordingly, in a preferred aspect, cellulosic material is subjected to mechanical, chemical, or physical pretreatment, or any combination thereof, to promote the separation and/or release of cellulose, hemicellulose, and/or lignin.
Biological Pretreatment: The term “biological pretreatment” refers to any biological pretreatment that promotes the separation and/or release of cellulose, hemicellulose, and/or lignin from cellulosic material. Biological pretreatment techniques can involve applying lignin-solubilizing microorganisms (see, for example, Hsu, T.-A., 1996, Pretreatment of biomass, in Handbook on Bioethanol: Production and Utilization, Wyman, C. E., ed., Taylor & Francis, Washington, D.C., 179-212; Ghosh and Singh, 1993, Physicochemical and biological treatments for enzymatic/microbial conversion of cellulosic biomass, Adv. Appl. Microbiol. 39: 295-333; McMillan, J. D., 1994, Pretreating lignocellulosic biomass: a review, in Enzymatic Conversion of Biomass for Fuels Production, Himmel, M. E., Baker, J. O., and Overend, R. P., eds., ACS Symposium Series 566, American Chemical Society, Washington, D.C., chapter 15; Gong, C. S., Cao, N. J., Du, J., and Tsao, G. T., 1999, Ethanol production from renewable resources, in Advances in Biochemical Engineering/Biotechnology, Scheper, T., ed., Springer-Verlag Berlin Heidelberg, Germany, 65: 207-241; Olsson and Hahn-Hagerdal, 1996, Fermentation of lignocellulosic hydrolysates for ethanol production, Enz. Microb. Tech. 18: 312-331; and Vallander and Eriksson, 1990, Production of ethanol from lignocellulosic materials: State of the art, Adv. Biochem. Eng./Biotechnol. 42: 63-95).
Saccharification. In the hydrolysis step, also known as saccharification, the pretreated cellulosic material is hydrolyzed to break down cellulose and alternatively also hemicellulose to fermentable sugars, such as glucose, cellobiose, xylose, xylulose, arabinose, mannose, galactose, and/or soluble oligosaccharides. The hydrolysis is performed enzymatically by an enzyme composition described herein. The enzymes of the compositions can also be added sequentially.
Enzymatic hydrolysis is preferably carried out in a suitable aqueous environment under conditions that can be readily determined by one skilled in the art. In a preferred aspect, hydrolysis is performed under conditions suitable for the activity of the enzyme(s), i.e., optimal for the enzyme(s). The hydrolysis can be carried out as a fed batch or continuous process where the pretreated cellulosic material (substrate) is fed gradually to, for example, an enzyme containing hydrolysis solution.
The saccharification is generally performed in stirred-tank reactors or fermentors under controlled pH, temperature, and mixing conditions. Suitable process time, temperature and pH conditions can readily be determined by one skilled in the art. For example, the saccharification can last up to 200 hours, but is typically performed for preferably about 12 to about 96 hours, more preferably about 16 to about 72 hours, and most preferably about 24 to about 48 hours. The temperature is in the range of preferably about 25° C. to about 70° C., more preferably about 30° C. to about 65° C., and more preferably about 40° C. to 60° C., in particular about 50° C. The pH is in the range of preferably about 3 to about 8, more preferably about 3.5 to about 7, and most preferably about 4 to about 6, in particular about pH 5. The dry solids content is in the range of preferably about 5 to about 50 wt %, more preferably about 10 to about 40 wt %, and most preferably about 20 to about 30 wt %.
The optimum amounts of the enzymes depend on several factors including, but not limited to, the mixture of component cellulolytic enzymes, the cellulosic substrate, the concentration of cellulosic substrate, the pretreatment(s) of the cellulosic substrate, temperature, time, pH, and inclusion of fermenting organism (e.g., yeast for Simultaneous Saccharification and Fermentation).
In a preferred aspect, an effective amount of cellulolytic enzyme(s) to cellulosic material is about 0.5 to about 50 mg, preferably at about 0.5 to about 40 mg, more preferably at about 0.5 to about 25 mg, more preferably at about 0.75 to about 20 mg, more preferably at about 0.75 to about 15 mg, even more preferably at about 0.5 to about 10 mg, and most preferably at about 2.5 to about 10 mg per g of cellulosic material.
In another preferred aspect, an effective amount of polypeptide(s) having cellulolytic enhancing activity to cellulosic material is about 0.01 to about 50.0 mg, preferably about 0.01 to about 40 mg, more preferably about 0.01 to about 30 mg, more preferably about 0.01 to about 20 mg, more preferably about 0.01 to about 10 mg, more preferably about 0.01 to about 5 mg, more preferably at about 0.025 to about 1.5 mg, more preferably at about 0.05 to about 1.25 mg, more preferably at about 0.075 to about 1.25 mg, more preferably at about 0.1 to about 1.25 mg, even more preferably at about 0.15 to about 1.25 mg, and most preferably at about 0.25 to about 1.0 mg per g of cellulosic material.
In another preferred aspect, an effective amount of polypeptide(s) having cellulolytic enhancing activity to cellulolytic protein(s) is about 0.005 to about 1.0 g, preferably at about 0.01 to about 1.0 g, more preferably at about 0.15 to about 0.75 g, more preferably at about 0.15 to about 0.5 g, more preferably at about 0.1 to about 0.5 g, even more preferably at about 0.1 to about 0.5 g, and most preferably at about 0.05 to about 0.2 g per g of cellulolytic protein(s).
Fermentation. The fermentable sugars obtained from the pretreated and hydrolyzed cellulosic material can be fermented by one or more (several) fermenting microorganisms capable of fermenting the sugars directly or indirectly into a desired fermentation product. “Fermentation” or “fermentation process” refers to any fermentation process or any process comprising a fermentation step. Fermentation processes also include fermentation processes used in the consumable alcohol industry (e.g., beer and wine), dairy industry (e.g., fermented dairy products), leather industry, and tobacco industry. The fermentation conditions depend on the desired fermentation product and fermenting organism and can easily be determined by one skilled in the art.
In the fermentation step, sugars, released from cellulosic material as a result of the pretreatment and enzymatic hydrolysis steps, are fermented to a product, e.g., ethanol, by a fermenting organism, such as yeast. Hydrolysis (saccharification) and fermentation can be separate or simultaneous, as described herein.
Any suitable hydrolyzed cellulosic material can be used in the fermentation step in practicing the present invention. The material is generally selected based on the desired fermentation product, i.e., the substance to be obtained from the fermentation, and the process employed, as is well known in the art.
The term “fermentation medium” is understood herein to refer to a medium before the fermenting microorganism(s) is(are) added, such as, a medium resulting from a saccharification process, as well as a medium used in a simultaneous saccharification and fermentation process (SSF).
“Fermenting microorganism” refers to any microorganism, including bacterial and fungal organisms, suitable for use in a desired fermentation process to produce a fermentation product. The fermenting organism can be C6 and/or C5 fermenting organisms, or a combination thereof. Both C6 and C5 fermenting organisms are well known in the art. Suitable fermenting microorganisms are able to ferment, i.e., convert, sugars, such as glucose, xylose, xylulose, arabinose, maltose, mannose, galactose, or oligosaccharides, directly or indirectly into the desired fermentation product.
Examples of bacterial and fungal fermenting organisms producing ethanol are described by Lin et al., 2006, Appl. Microbiol. Biotechnol. 69: 627-642.
Examples of fermenting microorganisms that can ferment C6 sugars include bacterial and fungal organisms, such as yeast. Preferred yeast includes strains of the Saccharomyces spp., preferably Saccharomyces cerevisiae. 
Examples of fermenting organisms that can ferment C5 sugars include bacterial and fungal organisms, such as yeast. Preferred C5 fermenting yeast include strains of Pichia, preferably Pichia stipitis, such as Pichia stipitis CBS 5773; strains of Candida, preferably Candida boidinii, Candida brassicae, Candida sheatae, Candida diddensii, Candida pseudotropicalis, or Candida utilis. 
Other fermenting organisms include strains of Zymomonas, such as Zymomonas mobilis; Hansenula, such as Hansenula anomala; Kluyveromyces, such as K. fragilis; Schizosaccharomyces, such as S. pombe; and E. coli, especially E. coli strains that have been genetically modified to improve the yield of ethanol.
In a preferred aspect, the yeast is a Saccharomyces spp. In a more preferred aspect, the yeast is Saccharomyces cerevisiae. In another more preferred aspect, the yeast is Saccharomyces distaticus. In another more preferred aspect, the yeast is Saccharomyces uvarum. In another preferred aspect, the yeast is a Kluyveromyces. In another more preferred aspect, the yeast is Kluyveromyces marxianus. In another more preferred aspect, the yeast is Kluyveromyces fragilis. In another preferred aspect, the yeast is a Candida. In another more preferred aspect, the yeast is Candida boidinii. In another more preferred aspect, the yeast is Candida brassicae. In another more preferred aspect, the yeast is Candida diddensii. In another more preferred aspect, the yeast is Candida pseudotropicalis. In another more preferred aspect, the yeast is Candida utilis. In another preferred aspect, the yeast is a Clavispora. In another more preferred aspect, the yeast is Clavispora lusitaniae. In another more preferred aspect, the yeast is Clavispora opuntiae. In another preferred aspect, the yeast is a Pachysolen. In another more preferred aspect, the yeast is Pachysolen tannophilus. In another preferred aspect, the yeast is a Pichia. In another more preferred aspect, the yeast is a Pichia stipitis. In another preferred aspect, the yeast is a Bretannomyces. In another more preferred aspect, the yeast is Bretannomyces clausenii (Philippidis, G. P., 1996, Cellulose bioconversion technology, in Handbook on Bioethanol: Production and Utilization, Wyman, C. E., ed., Taylor & Francis, Washington, D.C., 179-212).
Bacteria that can efficiently ferment hexose and pentose to ethanol include, for example, Zymomonas mobilis and Clostridium thermocellum (Philippidis, 1996, supra).
In a preferred aspect, the bacterium is a Zymomonas. In a more preferred aspect, the bacterium is Zymomonas mobilis. In another preferred aspect, the bacterium is a Clostridium. In another more preferred aspect, the bacterium is Clostridium thermocellum. 
Commercially available yeast suitable for ethanol production includes, e.g., ETHANOL REDTM yeast (available from Fermentis/Lesaffre, USA), FALITM (available from Fleischmann's Yeast, USA), SUPERSTARTTM and THERMOSACCTM fresh yeast (available from Ethanol Technology, WI, USA), BIOFERMTM AFT and XR (available from NABC—North American Bioproducts Corporation, GA, USA), GERT STRANDTM (available from Gert Strand AB, Sweden), and FERMIOLTM (available from DSM Specialties).
In a preferred aspect, the fermenting microorganism has been genetically modified to provide the ability to ferment pentose sugars, such as xylose utilizing, arabinose utilizing, and xylose and arabinose co-utilizing microorganisms.
The cloning of heterologous genes into various fermenting microorganisms has led to the construction of organisms capable of converting hexoses and pentoses to ethanol (cofermentation) (Chen and Ho, 1993, Cloning and improving the expression of Pichia stipitis xylose reductase gene in Saccharomyces cerevisiae, Appl. Biochem. Biotechnol. 39-40: 135-147; Ho et al., 1998, Genetically engineered Saccharomyces yeast capable of effectively cofermenting glucose and xylose, Appl. Environ. Microbiol. 64: 1852-1859; Kotter and Ciriacy, 1993, Xylose fermentation by Saccharomyces cerevisiae, Appl. Microbiol. Biotechnol. 38: 776-783; Walfridsson et al., 1995, Xylose-metabolizing Saccharomyces cerevisiae strains overexpressing the TKL1 and TAL1 genes encoding the pentose phosphate pathway enzymes transketolase and transaldolase, Appl. Environ. Microbiol. 61: 4184-4190; Kuyper et al., 2004, Minimal metabolic engineering of Saccharomyces cerevisiae for efficient anaerobic xylose fermentation: a proof of principle, FEMS Yeast Research 4: 655-664; Beall et al., 1991, Parametric studies of ethanol production from xylose and other sugars by recombinant Escherichia coli, Biotech. Bioeng. 38: 296-303; Ingram et al., 1998, Metabolic engineering of bacteria for ethanol production, Biotechnol. Bioeng. 58: 204-214; Zhang et al., 1995, Metabolic engineering of a pentose metabolism pathway in ethanologenic Zymomonas mobilis, Science 267: 240-243; Deanda et al., 1996, Development of an arabinose-fermenting Zymomonas mobilis strain by metabolic pathway engineering, Appl. Environ. Microbiol. 62: 4465-4470; WO 2003/062430, xylose isomerase).
In a preferred aspect, the genetically modified fermenting microorganism is Saccharomyces cerevisiae. In another preferred aspect, the genetically modified fermenting microorganism is Zymomonas mobilis. In another preferred aspect, the genetically modified fermenting microorganism is Escherichia coli. In another preferred aspect, the genetically modified fermenting microorganism is Klebsiella oxytoca. In another preferred aspect, the genetically modified fermenting microorganism is Kluyveromyces sp.
It is well known in the art that the organisms described above can also be used to produce other substances, as described herein.
The fermenting microorganism is typically added to the degraded lignocellulose or hydrolysate and the fermentation is performed for about 8 to about 96 hours, such as about 24 to about 60 hours. The temperature is typically between about 26° C. to about 60° C., in particular about 32° C. or 50° C., and at about pH 3 to about pH 8, such as around pH 4-5, 6, or 7.
In a preferred aspect, the yeast and/or another microorganism is applied to the degraded cellulosic material and the fermentation is performed for about 12 to about 96 hours, such as typically 24-60 hours. In a preferred aspect, the temperature is preferably between about 20° C. to about 60° C., more preferably about 25° C. to about 50° C., and most preferably about 32° C. to about 50° C., in particular about 32° C. or 50° C., and the pH is generally from about pH 3 to about pH 7, preferably around pH 4-7. However, some fermenting organisms, e.g., bacteria, have higher fermentation temperature optima. Yeast or another microorganism is preferably applied in amounts of approximately 105 to 1012, preferably from approximately 107 to 1010, especially approximately 2×108 viable cell count per ml of fermentation broth. Further guidance in respect of using yeast for fermentation can be found in, e.g., “The Alcohol Textbook” (Editors K. Jacques, T. P. Lyons and D. R. Kelsall, Nottingham University Press, United Kingdom 1999), which is hereby incorporated by reference.
For ethanol production, following the fermentation the fermented slurry is distilled to extract the ethanol. The ethanol obtained according to the methods of the invention can be used as, e.g., fuel ethanol, drinking ethanol, i.e., potable neutral spirits, or industrial ethanol.
A fermentation stimulator can be used in combination with any of the processes described herein to further improve the fermentation process, and in particular, the performance of the fermenting microorganism, such as, rate enhancement and ethanol yield. A “fermentation stimulator” refers to stimulators for growth of the fermenting microorganisms, in particular, yeast. Preferred fermentation stimulators for growth include vitamins and minerals. Examples of vitamins include multivitamins, biotin, pantothenate, nicotinic acid, meso-inositol, thiamine, pyridoxine, para-aminobenzoic acid, folic acid, riboflavin, and Vitamins A, B, C, D, and E. See, for example, Alfenore et al., Improving ethanol production and viability of Saccharomyces cerevisiae by a vitamin feeding strategy during fed-batch process, Springer-Verlag (2002), which is hereby incorporated by reference. Examples of minerals include minerals and mineral salts that can Supply nutrients comprising P, K, Mg, S, Ca, Fe, Zn, Mn, and Cu.
Fermentation products: A fermentation product can be any substance derived from the fermentation. The fermentation product can be, without limitation, an alcohol (e.g., arabinitol, butanol, ethanol, glycerol, methanol, 1,3-propanediol, sorbitol, and xylitol); an organic acid (e.g., acetic acid, acetonic acid, adipic acid, ascorbic acid, citric acid, 2,5-diketo-D-gluconic acid, formic acid, fumaric acid, glucaric acid, gluconic acid, glucuronic acid, glutaric acid, 3-hydroxypropionic acid, itaconic acid, lactic acid, malic acid, malonic acid, oxalic acid, oxaloacetic acid, propionic acid, succinic acid, and xylonic acid); a ketone (e.g., acetone); an amino acid (e.g., aspartic acid, glutamic acid, glycine, lysine, serine, and threonine); and a gas (e.g., methane, hydrogen (H2), carbon dioxide (CO2), and carbon monoxide (CO)). The fermentation product can also be protein as a high value product.
In a preferred aspect, the fermentation product is an alcohol. It will be understood that the term “alcohol” encompasses a substance that contains one or more hydroxyl moieties. In a more preferred aspect, the alcohol is arabinitol. In another more preferred aspect, the alcohol is butanol. In another more preferred aspect, the alcohol is ethanol. In another more preferred aspect, the alcohol is glycerol. In another more preferred aspect, the alcohol is methanol. In another more preferred aspect, the alcohol is 1,3-propanediol. In another more preferred aspect, the alcohol is sorbitol. In another more preferred aspect, the alcohol is xylitol. See, for example, Gong, C. S., Cao, N. J., Du, J., and Tsao, G. T., 1999, Ethanol production from renewable resources, in Advances in Biochemical Engineering/Biotechnology, Scheper, T., ed., Springer-Verlag Berlin Heidelberg, Germany, 65: 207-241; Silveira, M. M., and Jonas, R., 2002, The biotechnological production of sorbitol, Appl. Microbiol. Biotechnol. 59: 400-408; Nigam, P., and Singh, D., 1995, Processes for fermentative production of xylitol—a sugar substitute, Process Biochemistry 30 (2): 117-124; Ezeji, T. C., Qureshi, N. and Blaschek, H. P., 2003, Production of acetone, butanol and ethanol by Clostridium beijerinckii BA101 and in situ recovery by gas stripping, World Journal of Microbiology and Biotechnology 19 (6): 595-603.
In another preferred aspect, the fermentation product is an organic acid. In another more preferred aspect, the organic acid is acetic acid. In another more preferred aspect, the organic acid is acetonic acid. In another more preferred aspect, the organic acid is adipic acid. In another more preferred aspect, the organic acid is ascorbic acid. In another more preferred aspect, the organic acid is citric acid. In another more preferred aspect, the organic acid is 2,5-diketo-D-gluconic acid. In another more preferred aspect, the organic acid is formic acid. In another more preferred aspect, the organic acid is fumaric acid. In another more preferred aspect, the organic acid is glucaric acid. In another more preferred aspect, the organic acid is gluconic acid. In another more preferred aspect, the organic acid is glucuronic acid. In another more preferred aspect, the organic acid is glutaric acid. In another preferred aspect, the organic acid is 3-hydroxypropionic acid. In another more preferred aspect, the organic acid is itaconic acid. In another more preferred aspect, the organic acid is lactic acid. In another more preferred aspect, the organic acid is malic acid. In another more preferred aspect, the organic acid is malonic acid. In another more preferred aspect, the organic acid is oxalic acid. In another more preferred aspect, the organic acid is propionic acid. In another more preferred aspect, the organic acid is succinic acid. In another more preferred aspect, the organic acid is xylonic acid. See, for example, Chen, R., and Lee, Y. Y., 1997, Membrane-mediated extractive fermentation for lactic acid production from cellulosic biomass, Appl. Biochem. Biotechnol. 63-65: 435-448.
In another preferred aspect, the fermentation product is a ketone. It will be understood that the term “ketone” encompasses a substance that contains one or more ketone moieties. In another more preferred aspect, the ketone is acetone. See, for example, Qureshi and Blaschek, 2003, supra.
In another preferred aspect, the fermentation product is an amino acid. In another more preferred aspect, the organic acid is aspartic acid. In another more preferred aspect, the amino acid is glutamic acid. In another more preferred aspect, the amino acid is glycine. In another more preferred aspect, the amino acid is lysine. In another more preferred aspect, the amino acid is serine. In another more preferred aspect, the amino acid is threonine. See, for example, Richard, A., and Margaritis, A., 2004, Empirical modeling of batch fermentation kinetics for poly(glutamic acid) production and other microbial biopolymers, Biotechnology and Bioengineering 87 (4): 501-515.
In another preferred aspect, the fermentation product is a gas. In another more preferred aspect, the gas is methane. In another more preferred aspect, the gas is H2. In another more preferred aspect, the gas is CO2. In another more preferred aspect, the gas is CO. See, for example, Kataoka, N., A. Miya, and K. Kiriyama, 1997, Studies on hydrogen production by continuous culture system of hydrogen-producing anaerobic bacteria, Water Science and Technology 36 (6-7): 41-47; and Gunaseelan V. N. in Biomass and Bioenergy, Vol. 13 (1-2), pp. 83-114, 1997, Anaerobic digestion of biomass for methane production: A review.
Recovery. The fermentation product(s) can be optionally recovered from the fermentation medium using any method known in the art including, but not limited to, chromatography, electrophoretic procedures, differential solubility, distillation, or extraction. For example, alcohol is separated from the fermented cellulosic material and purified by conventional methods of distillation. Ethanol with a purity of up to about 96 vol. % can be obtained, which can be used as, for example, fuel ethanol, drinking ethanol, i.e., potable neutral spirits, or industrial ethanol.
Polypeptides Having Cellulolytic Enhancing Activity and Polynucleotides Thereof
In the methods of the present invention, any polypeptide having cellulolytic enhancing activity can be used.
In a first aspect, the polypeptide having cellulolytic enhancing activity comprises the following motifs:
[ILMV]-P-X(4,5)-G-X-Y-[ILMV]-X-R-X-[EQ]-X(4)-[HNQ] (SEQ ID NO: 71 or SEQ ID NO: 72) and [FW]-[TF]-K-[AIV],
wherein X is any amino acid, X(4,5) is any amino acid at 4 or 5 contiguous positions, and X(4) is any amino acid at 4 contiguous positions.
The polypeptide comprising the above-noted motifs may further comprise:
H-X(1,2)-G-P-X(3)-[YW]-[AILMV] (SEQ ID NO: 73 or SEQ ID NO: 74),
[EQ]-X-Y-X(2)-C-X-[EHQN]-[FILV]-X-[ILV] (SEQ ID NO: 75), or
H-X(1,2)-G-P-X(3)-[YW]-[AILMV] (SEQ ID NO: 76 or SEQ ID NO: 77) and [EQ]-X-Y-X(2)-C-X-[EHQN]-[FILV]-X-[ILV] (SEQ ID NO: 78),
wherein X is any amino acid, X(1,2) is any amino acid at 1 position or 2 contiguous positions, X(3) is any amino acid at 3 contiguous positions, and X(2) is any amino acid at 2 contiguous positions. In the above motifs, the accepted IUPAC single letter amino acid abbreviation is employed.
In a preferred aspect, the polypeptide having cellulolytic enhancing activity further comprises H-X(1,2)-G-P-X(3)-[YW]-[AILMV] (SEQ ID NO: 73 or SEQ ID NO: 74). In another preferred aspect, the isolated polypeptide having cellulolytic enhancing activity further comprises [EQ]-X-Y-X(2)-C-X-[EHQN]-[FILV]-X-[ILV] (SEQ ID NO: 75). In another preferred aspect, the polypeptide having cellulolytic enhancing activity further comprises H-X(1,2)-G-P-X(3)-[YW]-[AILMV] (SEQ ID NO: 76 or SEQ ID NO: 77) and [EQ]X-Y-X(2)-C-X-[EHQN]-[FILV]-X-[ILV] (SEQ ID NO: 78).
In a second aspect, the polypeptide having cellulolytic enhancing activity comprises the following motif:
[ILMV]-P-x(4,5)-G-x-Y-[ILMV]-x-R-x-[EQ]-x(3)-A-[HNQ] (SEQ ID NO: 79 or SEQ ID NO: 80),
wherein x is any amino acid, x(4,5) is any amino acid at 4 or 5 contiguous positions, and x(3) is any amino acid at 3 contiguous positions. In the above motif, the accepted IUPAC single letter amino acid abbreviation is employed.
In a third aspect, the polypeptide having cellulolytic enhancing activity comprises an amino acid sequence that has a degree of identity to the mature polypeptide of SEQ ID NO: 2, SEQ ID NO: 4, SEQ ID NO: 6, SEQ ID NO: 8, SEQ ID NO: 10, SEQ ID NO: 12, SEQ ID NO: 14, or SEQ ID NO: 16 of preferably at least 60%, more preferably at least 65%, more preferably at least 70%, more preferably at least 75%, more preferably at least 80%, more preferably at least 85%, even more preferably at least 90%, most preferably at least 95%, and even most preferably at least 96%, at least 97%, at least 98%, or at least 99% (hereinafter “homologous polypeptides”). In a preferred aspect, the mature polypeptide sequence is amino acids 20 to 326 of SEQ ID NO: 2, amino acids 18 to 239 of SEQ ID NO: 4, amino acids 20 to 258 of SEQ ID NO: 6, amino acids 19 to 226 of SEQ ID NO: 8, amino acids 20 to 304 of SEQ ID NO: 10, amino acids 16 to 317 of SEQ ID NO: 12, amino acids 23 to 250 of SEQ ID NO: 14, or amino acids 20 to 249 of SEQ ID NO: 16.
A polypeptide having cellulolytic enhancing activity preferably comprises the amino acid sequence of SEQ ID NO: 2 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In a preferred aspect, the polypeptide comprises the amino acid sequence of SEQ ID NO: 2. In another preferred aspect, the polypeptide comprises the mature polypeptide of SEQ ID NO: 2. In another preferred aspect, the polypeptide comprises amino acids 20 to 326 of SEQ ID NO: 2, or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide comprises amino acids 20 to 326 of SEQ ID NO: 2. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 2 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 2. In another preferred aspect, the polypeptide consists of the mature polypeptide of SEQ ID NO: 2. In another preferred aspect, the polypeptide consists of amino acids 20 to 326 of SEQ ID NO: 2 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of amino acids 20 to 326 of SEQ ID NO: 2.
A polypeptide having cellulolytic enhancing activity preferably comprises the amino acid sequence of SEQ ID NO: 4 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In a preferred aspect, the polypeptide comprises the amino acid sequence of SEQ ID NO: 4. In another preferred aspect, the polypeptide comprises the mature polypeptide of SEQ ID NO: 4. In another preferred aspect, the polypeptide comprises amino acids 18 to 239 of SEQ ID NO: 4, or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide comprises amino acids 18 to 239 of SEQ ID NO: 4. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 4 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 4. In another preferred aspect, the polypeptide consists of the mature polypeptide of SEQ ID NO: 4. In another preferred aspect, the polypeptide consists of amino acids 18 to 239 of SEQ ID NO: 4 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of amino acids 18 to 239 of SEQ ID NO: 4.
A polypeptide having cellulolytic enhancing activity preferably comprises the amino acid sequence of SEQ ID NO: 6 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In a preferred aspect, the polypeptide comprises the amino acid sequence of SEQ ID NO: 6. In another preferred aspect, the polypeptide comprises the mature polypeptide of SEQ ID NO: 6. In another preferred aspect, the polypeptide comprises amino acids 20 to 258 of SEQ ID NO: 6, or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide comprises amino acids 20 to 258 of SEQ ID NO: 6. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 6 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 6. In another preferred aspect, the polypeptide consists of the mature polypeptide of SEQ ID NO: 6. In another preferred aspect, the polypeptide consists of amino acids 20 to 258 of SEQ ID NO: 6 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of amino acids 20 to 258 of SEQ ID NO: 6.
A polypeptide having cellulolytic enhancing activity preferably comprises the amino acid sequence of SEQ ID NO: 8 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In a preferred aspect, the polypeptide comprises the amino acid sequence of SEQ ID NO: 8. In another preferred aspect, the polypeptide comprises the mature polypeptide of SEQ ID NO: 8. In another preferred aspect, the polypeptide comprises amino acids 19 to 226 of SEQ ID NO: 8, or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide comprises amino acids 19 to 226 of SEQ ID NO: 8. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 8 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 8. In another preferred aspect, the polypeptide consists of the mature polypeptide of SEQ ID NO: 8. In another preferred aspect, the polypeptide consists of amino acids 19 to 226 of SEQ ID NO: 8 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of amino acids 19 to 226 of SEQ ID NO: 8.
A polypeptide having cellulolytic enhancing activity preferably comprises the amino acid sequence of SEQ ID NO: 10 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In a preferred aspect, the polypeptide comprises the amino acid sequence of SEQ ID NO: 10. In another preferred aspect, the polypeptide comprises the mature polypeptide of SEQ ID NO: 10. In another preferred aspect, the polypeptide comprises amino acids 20 to 304 of SEQ ID NO: 10, or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide comprises amino acids 20 to 304 of SEQ ID NO: 10. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 10 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 10. In another preferred aspect, the polypeptide consists of the mature polypeptide of SEQ ID NO: 10. In another preferred aspect, the polypeptide consists of amino acids 20 to 304 of SEQ ID NO: 10 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of amino acids 20 to 304 of SEQ ID NO: 10.
A polypeptide having cellulolytic enhancing activity preferably comprises the amino acid sequence of SEQ ID NO: 12 or an allelic variant thereof; or a fragment thereof having cellulolytic enhancing activity. In a preferred aspect, the polypeptide comprises the amino acid sequence of SEQ ID NO: 12. In another preferred aspect, the polypeptide comprises the mature polypeptide of SEQ ID NO: 12. In another preferred aspect, the polypeptide comprises amino acids 16 to 317 of SEQ ID NO: 12, or an allelic variant thereof; or a fragment thereof having cellulolytic enhancing activity. In another preferred aspect, the polypeptide comprises amino acids 16 to 317 of SEQ ID NO: 12. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 12 or an allelic variant thereof; or a fragment thereof having cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 12. In another preferred aspect, the polypeptide consists of the mature polypeptide of SEQ ID NO: 12. In another preferred aspect, the polypeptide consists of amino acids 16 to 317 of SEQ ID NO: 12 or an allelic variant thereof; or a fragment thereof having cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of amino acids 16 to 317 of SEQ ID NO: 12.
A polypeptide having cellulolytic enhancing activity preferably comprises the amino acid sequence of SEQ ID NO: 14 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In a preferred aspect, the polypeptide comprises the amino acid sequence of SEQ ID NO: 14. In another preferred aspect, the polypeptide comprises the mature polypeptide of SEQ ID NO: 14. In another preferred aspect, the polypeptide comprises amino acids 23 to 250 of SEQ ID NO: 14, or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide comprises amino acids 23 to 250 of SEQ ID NO: 14. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 14 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 14. In another preferred aspect, the polypeptide consists of the mature polypeptide of SEQ ID NO: 14. In another preferred aspect, the polypeptide consists of amino acids 23 to 250 of SEQ ID NO: 14 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of amino acids 23 to 250 of SEQ ID NO: 14.
A polypeptide having cellulolytic enhancing activity preferably comprises the amino acid sequence of SEQ ID NO: 16 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In a preferred aspect, the polypeptide comprises the amino acid sequence of SEQ ID NO: 16. In another preferred aspect, the polypeptide comprises the mature polypeptide of SEQ ID NO: 16. In another preferred aspect, the polypeptide comprises amino acids 20 to 249 of SEQ ID NO: 16, or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide comprises amino acids 20 to 249 of SEQ ID NO: 16. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 16 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of the amino acid sequence of SEQ ID NO: 16. In another preferred aspect, the polypeptide consists of the mature polypeptide of SEQ ID NO: 16. In another preferred aspect, the polypeptide consists of amino acids 20 to 249 of SEQ ID NO: 16 or an allelic variant thereof; or a fragment thereof that has cellulolytic enhancing activity. In another preferred aspect, the polypeptide consists of amino acids 20 to 249 of SEQ ID NO: 16.
Preferably, a fragment of the mature polypeptide of SEQ ID NO: 2 contains at least 277 amino acid residues, more preferably at least 287 amino acid residues, and most preferably at least 297 amino acid residues. Preferably, a fragment of the mature polypeptide of SEQ ID NO: 4 contains at least 185 amino acid residues, more preferably at least 195 amino acid residues, and most preferably at least 205 amino acid residues. Preferably, a fragment of the mature polypeptide of SEQ ID NO: 6 contains at least 200 amino acid residues, more preferably at least 212 amino acid residues, and most preferably at least 224 amino acid residues. Preferably, a fragment of the mature polypeptide of SEQ ID NO: 8 contains at least 175 amino acid residues, more preferably at least 185 amino acid residues, and most preferably at least 195 amino acid residues. Preferably, a fragment of the mature polypeptide of SEQ ID NO: 10 contains at least 240 amino acid residues, more preferably at least 255 amino acid residues, and most preferably at least 270 amino acid residues. Preferably, a fragment of the mature polypeptide of SEQ ID NO: 12 contains at least 255 amino acid residues, more preferably at least 270 amino acid residues, and most preferably at least 285 amino acid residues. Preferably, a fragment of the mature polypeptide of SEQ ID NO: 14 contains at least 175 amino acid residues, more preferably at least 190 amino acid residues, and most preferably at least 205 amino acid residues. Preferably, a fragment of the mature polypeptide of SEQ ID NO: 16 contains at least 200 amino acid residues, more preferably at least 210 amino acid residues, and most preferably at least 220 amino acid residues.
Preferably, a subsequence of the mature polypeptide coding sequence of SEQ ID NO: 1 contains at least 831 nucleotides, more preferably at least 861 nucleotides, and most preferably at least 891 nucleotides. Preferably, a subsequence of the mature polypeptide coding sequence of SEQ ID NO: 3 contains at least 555 nucleotides, more preferably at least 585 nucleotides, and most preferably at least 615 nucleotides. Preferably, a subsequence of the mature polypeptide coding sequence of SEQ ID NO: 5 contains at least 600 nucleotides, more preferably at least 636 nucleotides, and most preferably at least 672 nucleotides. Preferably, a subsequence of the mature polypeptide coding sequence of SEQ ID NO: 7 contains at least 525 nucleotides, more preferably at least 555 nucleotides, and most preferably at least 585 nucleotides. Preferably, a subsequence of the mature polypeptide coding sequence of SEQ ID NO: 9 contains at least 720 nucleotides, more preferably at least 765 nucleotides, and most preferably at least 810 nucleotides. Preferably, a subsequence of the mature polypeptide coding sequence of SEQ ID NO: 11 contains at least 765 nucleotides, more preferably at least 810 nucleotides, and most preferably at least 855 nucleotides Preferably, a subsequence of the mature polypeptide coding sequence of nucleotides 67 to 796 of SEQ ID NO: 13 contains at least 525 nucleotides, more preferably at least 570 nucleotides, and most preferably at least 615 nucleotides. Preferably, a subsequence of the mature polypeptide coding sequence of SEQ ID NO: 15 contains at least 600 nucleotides, more preferably at least 630 nucleotides, and most preferably at least 660 nucleotides.
In a fourth aspect, the polypeptide having cellulolytic enhancing activity is encoded by a polynucleotide that hybridizes under at least very low stringency conditions, preferably at least low stringency conditions, more preferably at least medium stringency conditions, more preferably at least medium-high stringency conditions, even more preferably at least high stringency conditions, and most preferably at least very high stringency conditions with (i) the mature polypeptide coding sequence of SEQ ID NO: 1, SEQ ID NO: 3, SEQ ID NO: 5, SEQ ID NO: 7, SEQ ID NO: 9, SEQ ID NO: 11, SEQ ID NO: 13, or SEQ ID NO: 15, (ii) the cDNA sequence contained in the mature polypeptide coding sequence of SEQ ID NO: 1, SEQ ID NO: 3, SEQ ID NO: 5, or SEQ ID NO: 13, or the genomic DNA sequence comprising the mature polypeptide coding sequence of SEQ ID NO: 7, SEQ ID NO: 9, SEQ ID NO: 11, or SEQ ID NO: 15, (iii) a subsequence of (i) or (ii), or (iv) a full-length complementary strand of (i), (ii), or (iii) (J. Sambrook, E. F. Fritsch, and T. Maniatus, 1989, supra). A subsequence of the mature polypeptide coding sequence of SEQ ID NO: 1, SEQ ID NO: 3, SEQ ID NO: 5, SEQ ID NO: 7, SEQ ID NO: 9, SEQ ID NO: 11, SEQ ID NO: 13, or SEQ ID NO: 15 contains at least 100 contiguous nucleotides or preferably at least 200 contiguous nucleotides. Moreover, the subsequence may encode a polypeptide fragment that has cellulolytic enhancing activity. In a preferred aspect, the mature polypeptide coding sequence is nucleotides 388 to 1332 of SEQ ID NO: 1, nucleotides 98 to 821 of SEQ ID NO: 3, nucleotides 126 to 978 of SEQ ID NO: 5, nucleotides 55 to 678 of SEQ ID NO: 7, nucleotides 58 to 912 of SEQ ID NO: 9, nucleotides 46 to 951 of SEQ ID NO: 11, nucleotides 67 to 796 of SEQ ID NO: 13, or nucleotides 77 to 766 of SEQ ID NO: 15.
The nucleotide sequence of SEQ ID NO: 1, SEQ ID NO: 3, SEQ ID NO: 5, SEQ ID NO: 7, SEQ ID NO: 9, SEQ ID NO: 11, SEQ ID NO: 13, or SEQ ID NO: 15, or a subsequence thereof; as well as the amino acid sequence of SEQ ID NO: 2, SEQ ID NO: 4, SEQ ID NO: 6, SEQ ID NO: 8, SEQ ID NO: 10, SEQ ID NO: 12, SEQ ID NO: 14, or SEQ ID NO: 16, or a fragment thereof, may be used to design a nucleic acid probe to identify and clone DNA encoding polypeptides having cellulolytic enhancing activity from strains of different genera or species according to methods well known in the art. In particular, such probes can be used for hybridization with the genomic or cDNA of the genus or species of interest, following standard Southern blotting procedures, in order to identify and isolate the corresponding gene therein. Such probes can be considerably shorter than the entire sequence, but should be at least 14, preferably at least 25, more preferably at least 35, and most preferably at least 70 nucleotides in length. It is, however, preferred that the nucleic acid probe is at least 100 nucleotides in length. For example, the nucleic acid probe may be at least 200 nucleotides, preferably at least 300 nucleotides, more preferably at least 400 nucleotides, or most preferably at least 500 nucleotides in length. Even longer probes may be used, e.g., nucleic acid probes that are preferably at least 600 nucleotides, more preferably at least 700 nucleotides, even more preferably at least 800 nucleotides, or most preferably at least 900 nucleotides in length. Both DNA and RNA probes can be used. The probes are typically labeled for detecting the corresponding gene (for example, with 32P, 3H, 35S, biotin, or avidin). Such probes are encompassed by the present invention.
A genomic DNA or cDNA library prepared from such other strains may, therefore, be screened for DNA that hybridizes with the probes described above and encodes a polypeptide having cellulolytic enhancing activity. Genomic or other DNA from such other strains may be separated by agarose or polyacrylamide gel electrophoresis, or other separation techniques. DNA from the libraries or the separated DNA may be transferred to and immobilized on nitrocellulose or other suitable carrier material. In order to identify a clone or DNA that is homologous with SEQ ID NO: 1, or a subsequence thereof, the carrier material is preferably used in a Southern blot.
For purposes of the present invention, hybridization indicates that the nucleotide sequence hybridizes to a labeled nucleic acid probe corresponding to the mature polypeptide coding sequence of SEQ ID NO: 1, SEQ ID NO: 3, SEQ ID NO: 5, SEQ ID NO: 7, SEQ ID NO: 9, SEQ ID NO: 11, SEQ ID NO: 13, or SEQ ID NO: 15 the cDNA sequence contained in the mature polypeptide coding sequence of SEQ ID NO: 1, SEQ ID NO: 3, SEQ ID NO: 5, or SEQ ID NO: 13, or the genomic DNA sequence comprising the mature polypeptide coding sequence of SEQ ID NO: 7, SEQ ID NO: 9, SEQ ID NO: 11, or SEQ ID NO: 15, its full-length complementary strand, or a subsequence thereof, under very low to very high stringency conditions, as described supra.
In a preferred aspect, the nucleic acid probe is the mature polypeptide coding sequence of SEQ ID NO: 1. In another preferred aspect, the nucleic acid probe is nucleotides 388 to 1332 of SEQ ID NO: 1. In another preferred aspect, the nucleic acid probe is a polynucleotide sequence that encodes the polypeptide of SEQ ID NO: 2, or a subsequence thereof. In another preferred aspect, the nucleic acid probe is SEQ ID NO: 1. In another preferred aspect, the nucleic acid probe is the polynucleotide sequence contained in plasmid pEJG120 which is contained in E. coli NRRL B-30699, wherein the polynucleotide sequence thereof encodes a polypeptide having cellulolytic enhancing activity. In another preferred aspect, the nucleic acid probe is the mature polypeptide coding sequence contained in plasmid pEJG120 which is contained in E. coli NRRL B-30699.
In another preferred aspect, the nucleic acid probe is the mature polypeptide coding sequence of SEQ ID NO: 3. In another preferred aspect, the nucleic acid probe is nucleotides 98 to 821 of SEQ ID NO: 3. In another preferred aspect, the nucleic acid probe is a polynucleotide sequence that encodes the polypeptide of SEQ ID NO: 4, or a subsequence thereof. In another preferred aspect, the nucleic acid probe is SEQ ID NO: 3. In another preferred aspect, the nucleic acid probe is the polynucleotide sequence contained in plasmid pTter61C which is contained in E. coli NRRL B-30813, wherein the polynucleotide sequence thereof encodes a polypeptide having cellulolytic enhancing activity. In another preferred aspect, the nucleic acid probe is the mature polypeptide coding sequence contained in plasmid pTter61C which is contained in E. coli NRRL B-30813.
In another preferred aspect, the nucleic acid probe is the mature polypeptide coding sequence of SEQ ID NO: 5. In another preferred aspect, the nucleic acid probe is nucleotides 126 to 978 of SEQ ID NO: 5. In another preferred aspect, the nucleic acid probe is a polynucleotide sequence that encodes the polypeptide of SEQ ID NO: 6, or a subsequence thereof. In another preferred aspect, the nucleic acid probe is SEQ ID NO: 5. In another preferred aspect, the nucleic acid probe is the polynucleotide sequence contained in plasmid pTter61D which is contained in E. coli NRRL B-30812, wherein the polynucleotide sequence thereof encodes a polypeptide having cellulolytic enhancing activity. In another preferred aspect, the nucleic acid probe is the mature polypeptide coding sequence contained in plasmid pTter61D which is contained in E. coli NRRL B-30812.
In another preferred aspect, the nucleic acid probe is the mature polypeptide coding sequence of SEQ ID NO: 7. In another preferred aspect, the nucleic acid probe is nucleotides 55 to 678 of SEQ ID NO: 7. In another preferred aspect, the nucleic acid probe is a polynucleotide sequence that encodes the polypeptide of SEQ ID NO: 8, or a subsequence thereof. In another preferred aspect, the nucleic acid probe is SEQ ID NO: 7. In another preferred aspect, the nucleic acid probe is the polynucleotide sequence contained in plasmid pTter61E which is contained in E. coli NRRL B-30814, wherein the polynucleotide sequence thereof encodes a polypeptide having cellulolytic enhancing activity. In another preferred aspect, the nucleic acid probe is the mature polypeptide coding sequence contained in plasmid pTter61E which is contained in E. coli NRRL B-30814.
In another preferred aspect, the nucleic acid probe is the mature polypeptide coding sequence of SEQ ID NO: 9. In another preferred aspect, the nucleic acid probe is nucleotides 58 to 912 of SEQ ID NO: 9 In another preferred aspect, the nucleic acid probe is a polynucleotide sequence that encodes the polypeptide of SEQ ID NO: 10, or a subsequence thereof. In another preferred aspect, the nucleic acid probe is SEQ ID NO: 9. In another preferred aspect, the nucleic acid probe is the polynucleotide sequence contained in plasmid pTter61G which is contained in E. coli NRRL B-30811, wherein the polynucleotide sequence thereof encodes a polypeptide having cellulolytic enhancing activity. In another preferred aspect, the nucleic acid probe is the mature polypeptide coding sequence contained in plasmid pTter61G which is contained in E. coli NRRL B-30811.
In another preferred aspect, the nucleic acid probe is the mature polypeptide coding sequence of SEQ ID NO: 11. In another preferred aspect, the nucleic acid probe is nucleotides 46 to 951 of SEQ ID NO: 11. In another preferred aspect, the nucleic acid probe is a polynucleotide sequence that encodes the polypeptide of SEQ ID NO: 12, or a subsequence thereof. In another preferred aspect, the nucleic acid probe is SEQ ID NO: 11. In another preferred aspect, the nucleic acid probe is the polynucleotide sequence contained in plasmid pTter61F which is contained in E. coli NRRL B-50044, wherein the polynucleotide sequence thereof encodes a polypeptide having cellulolytic enhancing activity. In another preferred aspect, the nucleic acid probe is the mature polypeptide coding region contained in plasmid pTter61F which is contained in E. coli NRRL B-50044.
In another preferred aspect, the nucleic acid probe is the mature polypeptide coding sequence of SEQ ID NO: 13. In another preferred aspect, the nucleic acid probe is nucleotides 67 to 796 of SEQ ID NO: 13. In another preferred aspect, the nucleic acid probe is a polynucleotide sequence that encodes the polypeptide of SEQ ID NO: 14, or a subsequence thereof. In another preferred aspect, the nucleic acid probe is SEQ ID NO: 13. In another preferred aspect, the nucleic acid probe is the polynucleotide sequence contained in plasmid pDZA2-7 which is contained in E. coli NRRL B-30704, wherein the polynucleotide sequence thereof encodes a polypeptide having cellulolytic enhancing activity. In another preferred aspect, the nucleic acid probe is the mature polypeptide coding sequence contained in plasmid pDZA2-7 which is contained in E. coli NRRL B-30704.
In another preferred aspect, the nucleic acid probe is the mature polypeptide coding sequence of SEQ ID NO: 15. In another preferred aspect, the nucleic acid probe is nucleotides 77 to 766 of SEQ ID NO: 15. In another preferred aspect, the nucleic acid probe is a polynucleotide sequence that encodes the polypeptide of SEQ ID NO: 16, or a subsequence thereof. In another preferred aspect, the nucleic acid probe is SEQ ID NO: 15. In another preferred aspect, the nucleic acid probe is the polynucleotide sequence contained in plasmid pTr333 which is contained in E. coli NRRL B-30878, wherein the polynucleotide sequence thereof encodes a polypeptide having cellulolytic enhancing activity. In another preferred aspect, the nucleic acid probe is the mature polypeptide coding sequence contained in plasmid pTr333 which is contained in E. coli NRRL B-30878.
For long probes of at least 100 nucleotides in length, very low to very high stringency conditions are defined as prehybridization and hybridization at 42° C. in 5×SSPE, 0.3% SDS, 200 μg/ml sheared and denatured salmon sperm DNA, and either 25% formamide for very low and low stringencies, 35% formamide for medium and medium-high stringencies, or 50% formamide for high and very high stringencies, following standard Southern blotting procedures for 12 to 24 hours optimally.
For long probes of at least 100 nucleotides in length, the carrier material is finally washed three times each for 15 minutes using 2×SSC, 0.2% SDS preferably at 45° C. (very low stringency), more preferably at 50° C. (low stringency), more preferably at 55° C. (medium stringency), more preferably at 60° C. (medium-high stringency), even more preferably at 65° C. (high stringency), and most preferably at 70° C. (very high stringency).
For short probes of about 15 nucleotides to about 70 nucleotides in length, stringency conditions are defined as prehybridization, hybridization, and washing post-hybridization at about 5° C. to about 10° C. below the calculated Tm, using the calculation according to Bolton and McCarthy (1962, Proceedings of the National Academy of Sciences USA 48:1390) in 0.9 M NaCl, 0.09 M Tris-HCl pH 7.6, 6 mM EDTA, 0.5% NP-40, 1×Denhardt's solution, 1 mM sodium pyrophosphate, 1 mM sodium monobasic phosphate, 0.1 mM ATP, and 0.2 mg of yeast RNA per ml following standard Southern blotting procedures for 12 to 24 hours optimally.
For short probes of about 15 nucleotides to about 70 nucleotides in length, the carrier material is washed once in 6×SCC plus 0.1% SDS for 15 minutes and twice each for 15 minutes using 6×SSC at 5° C. to 10° C. below the calculated Tm.
In a fifth aspect, the polypeptide having cellulolytic enhancing activity is encoded by a polynucleotide comprising or consisting of a nucleotide sequence that has a degree of identity to the mature polypeptide coding sequence of SEQ ID NO: 1, SEQ ID NO: 3, SEQ ID NO: 5, SEQ ID NO: 7, SEQ ID NO: 9, SEQ ID NO: 11, SEQ ID NO: 13, or SEQ ID NO: 15 of preferably at least 60%, more preferably at least 65%, more preferably at least 70%, more preferably at least 75%, more preferably at least 80%, more preferably at least 85%, even more preferably at least 90%, most preferably at least 95%, and even most preferably at least 96%, at least 97%, at least 98%, or at least 99%.
In a preferred aspect, the mature polypeptide coding sequence is nucleotides 388 to 1332 of SEQ ID NO: 1, nucleotides 98 to 821 of SEQ ID NO: 3, nucleotides 126 to 978 of SEQ ID NO: 5, nucleotides 55 to 678 of SEQ ID NO: 7, nucleotides 58 to 912 of SEQ ID NO: 9, nucleotides 46 to 951 of SEQ ID NO: 11, nucleotides 67 to 796 of SEQ ID NO: 13, or nucleotides 77 to 766 of SEQ ID NO: 15.
In a sixth aspect, the polypeptide having cellulolytic enhancing activity is an artificial variant comprising a substitution, deletion, and/or insertion of one or more (or several) amino acids of the mature polypeptide of SEQ ID NO: 2, SEQ ID NO: 4, SEQ ID NO: 6, SEQ ID NO: 8, SEQ ID NO: 10, SEQ ID NO: 12, or SEQ ID NO: 14, or SEQ ID NO: 16; or a homologous sequence thereof. Methods for preparing such an artificial variant is described supra.
The total number of amino acid substitutions, deletions and/or insertions of the mature polypeptide of SEQ ID NO: 2, SEQ ID NO: 4, SEQ ID NO: 6, SEQ ID NO: 8, SEQ ID NO: 10, SEQ ID NO: 12, or SEQ ID NO: 14, or SEQ ID NO: 16, is 10, preferably 9, more preferably 8, more preferably 7, more preferably at most 6, more preferably 5, more preferably 4, even more preferably 3, most preferably 2, and even most preferably 1.
A polypeptide having cellulolytic enhancing activity may be obtained from microorganisms of any genus. In a preferred aspect, the polypeptide obtained from a given source is secreted extracellularly.
A polypeptide having cellulolytic enhancing activity may be a bacterial polypeptide. For example, the polypeptide may be a gram positive bacterial polypeptide such as a Bacillus, Streptococcus, Streptomyces, Staphylococcus, Enterococcus, Lactobacillus, Lactococcus, Clostridium, Geobacillus, or Oceanobacillus polypeptide having cellulolytic enhancing activity, or a Gram negative bacterial polypeptide such as an E. coli, Pseudomonas, Salmonella, Campylobacter, Helicobacter, Flavobacterium, Fusobacterium, Ilyobacter, Neisseria, or Ureaplasma polypeptide having cellulolytic enhancing activity.
In a preferred aspect, the polypeptide is a Bacillus alkalophilus, Bacillus amyloliquefaciens, Bacillus brevis, Bacillus circulans, Bacillus clausii, Bacillus coagulans, Bacillus firmus, Bacillus lautus, Bacillus lentus, Bacillus licheniformis, Bacillus megaterium, Bacillus pumilus, Bacillus stearothermophilus, Bacillus subtilis, or Bacillus thuringiensis polypeptide having cellulolytic enhancing activity.
In another preferred aspect, the polypeptide is a Streptococcus equisimilis, Streptococcus pyogenes, Streptococcus uberis, or Streptococcus equi subsp. Zooepidemicus polypeptide having cellulolytic enhancing activity.
In another preferred aspect, the polypeptide is a Streptomyces achromogenes, Streptomyces avermitilis, Streptomyces coelicolor, Streptomyces griseus, or Streptomyces lividans polypeptide having cellulolytic enhancing activity.
The polypeptide having cellulolytic enhancing activity may also be a fungal polypeptide, and more preferably a yeast polypeptide such as a Candida, Kluyveromyces, Pichia, Saccharomyces, Schizosaccharomyces, or Yarrowia polypeptide having cellulolytic enhancing activity; or more preferably a filamentous fungal polypeptide such as aan Acremonium, Agaricus, Alternaria, Aspergillus, Aureobasidium, Botryospaeria, Ceriporiopsis, Chaetomidium, Chrysosporium, Claviceps, Cochliobolus, Coprinopsis, Coptotermes, Corynascus, Cryphonectria, Cryptococcus, Diplodia, Exidia, Filibasidium, Fusarium, Gibberella, Holomastigotoides, Humicola, Irpex, Lentinula, Leptospaeria, Magnaporthe, Melanocarpus, Meripilus, Mucor, Myceliophthora, Neocallimastix, Neurospora, Paecilomyces, Penicillium, Phanerochaete, Piromyces, Poitrasia, Pseudoplectania, Pseudotrichonympha, Rhizomucor, Schizophyllum, Scytalidium, Talaromyces, Thermoascus, Thielavia, Tolypocladium, Trichoderma, Trichophaea, Verticillium, Volvariella, or Xylaria polypeptide having cellulolytic enhancing activity.
In a preferred aspect, the polypeptide is a Saccharomyces carlsbergensis, Saccharomyces cerevisiae, Saccharomyces diastaticus, Saccharomyces douglasii, Saccharomyces kluyveri, Saccharomyces norbensis, or Saccharomyces oviformis polypeptide having cellulolytic enhancing activity.
In another preferred aspect, the polypeptide is an Acremonium cellulolyticus, Aspergillus aculeatus, Aspergillus awamori, Aspergillus fumigatus, Aspergillus foetidus, Aspergillus japonicus, Aspergillus nidulans, Aspergillus niger, Aspergillus oryzae, Chrysosporium keratinophilum, Chrysosporium lucknowense, Chrysosporium tropicum, Chrysosporium merdarium, Chrysosporium inops, Chrysosporium pannicola, Chrysosporium queenslandicum, Chrysosporium zonatum, Fusarium bactridioides, Fusarium cerealis, Fusarium crookwellense, Fusarium culmorum, Fusarium graminearum, Fusarium graminum, Fusarium heterosporum, Fusarium negundi, Fusarium oxysporum, Fusarium reticulatum, Fusarium roseum, Fusarium sambucinum, Fusarium sarcochroum, Fusarium sporotrichioides, Fusarium sulphureum, Fusarium torulosum, Fusarium trichothecioides, Fusarium venenatum, Humicola grisea, Humicola insolens, Humicola lanuginosa, Irpex lacteus, Mucor miehei, Myceliophthora thermophila, Neurospora crassa, Penicillium funiculosum, Penicillium purpurogenum, Phanerochaete chrysosporium, Thielavia achromatica, Thielavia albomyces, Thielavia albopilosa, Thielavia australeinsis, Thielavia fimeti, Thielavia microspora, Thielavia ovispora, Thielavia peruviana, Thielavia spededonium, Thielavia setosa, Thielavia subthermophila, Thielavia terrestris, Trichoderma harzianum, Trichoderma koningii, Trichoderma longibrachiatum, Trichoderma reesei, Trichoderma viride, or Trichophaea saccata polypeptide having cellulolytic enhancing activity.
It will be understood that for the aforementioned species the invention encompasses both the perfect and imperfect states, and other taxonomic equivalents, e.g., anamorphs, regardless of the species name by which they are known. Those skilled in the art will readily recognize the identity of appropriate equivalents.
Strains of these species are readily accessible to the public in a number of culture collections, such as the American Type Culture Collection (ATCC), Deutsche Sammlung von Mikroorganismen and Zellkulturen GmbH (DSM), Centraalbureau Voor Schimmelcultures (CBS), and Agricultural Research Service Patent Culture Collection, Northern Regional Research Center (NRRL).
Furthermore, polypeptides having cellulolytic enhancing activity may be identified and obtained from other sources including microorganisms isolated from nature (e.g., soil, composts, water, etc.) using the above-mentioned probes. Techniques for isolating microorganisms from natural habitats are well known in the art. The polynucleotide may then be obtained by similarly screening a genomic or cDNA library of such a microorganism. Once a polynucleotide encoding a polypeptide has been detected with the probe(s), the polynucleotide can be isolated or cloned by utilizing techniques that are well known to those of ordinary skill in the art (see, e.g., Sambrook et al., 1989, supra)
Polynucleotides comprising nucleotide sequences that encode polypeptide having cellulolytic enhancing activity can be isolated and utilized to express the polypeptide having cellulolytic enhancing activity for evaluation in the methods of the present invention, as described herein.
The polynucleotides comprise nucleotide sequences that have a degree of identity to the mature polypeptide coding sequence of SEQ ID NO: 1, SEQ ID NO: 3, SEQ ID NO: 5, SEQ ID NO: 7, SEQ ID NO: 9, SEQ ID NO: 11, SEQ ID NO: 13, or SEQ ID NO: 15 of preferably at least 60%, more preferably at least 65%, more preferably at least 70%, more preferably at least 75%, more preferably at least 80%, more preferably at least 85%, even more preferably at least 90%, most preferably at least 95%, and even most preferably at least 96%, at least 97%, at least 98%, or at least 99%, which encode a polypeptide having cellulolytic enhancing activity.
The polynucleotide may also be a polynucleotide encoding a polypeptide having cellulolytic enhancing activity that hybridizes under at least very low stringency conditions, preferably at least low stringency conditions, more preferably at least medium stringency conditions, more preferably at least medium-high stringency conditions, even more preferably at least high stringency conditions, and most preferably at least very high stringency conditions with (i) t the mature polypeptide coding sequence of SEQ ID NO: 1, SEQ ID NO: 3, SEQ ID NO: 5, SEQ ID NO: 7, SEQ ID NO: 9, SEQ ID NO: 11, SEQ ID NO: 13, or SEQ ID NO: 15, (ii) the cDNA sequence contained in the mature polypeptide coding sequence of SEQ ID NO: 1, SEQ ID NO: 3, SEQ ID NO: 5, or SEQ ID NO: 13, or the genomic DNA sequence comprising the mature polypeptide coding sequence of SEQ ID NO: 7, SEQ ID NO: 9, SEQ ID NO: 11, or SEQ ID NO: 15, or (iii) a full-length complementary strand of (i) or (ii); or allelic variants and subsequences thereof (Sambrook et al., 1989, supra), as defined herein. In a preferred aspect, the mature polypeptide coding sequence is nucleotides 388 to 1332 of SEQ ID NO: 1, nucleotides 98 to 821 of SEQ ID NO: 3, nucleotides 126 to 978 of SEQ ID NO: 5, nucleotides 55 to 678 of SEQ ID NO: 7, nucleotides 58 to 912 of SEQ ID NO: 9, nucleotides 46 to 951 of SEQ ID NO: 11, nucleotides 67 to 796 of SEQ ID NO: 13, or nucleotides 77 to 766 of SEQ ID NO: 15.
As described earlier, the techniques used to isolate or clone a polynucleotide encoding a polypeptide are known in the art and include isolation from genomic DNA, preparation from cDNA, or a combination thereof.
Cellobiose Dehydrogenases and Polynucleotides Thereof
In the present invention, a cellobiose dehydrogenase may be present as an enzyme activity in the enzyme composition and/or as a component of one or more protein components added to the composition. The cellobiose dehydrogenase can be any cellobiose dehydrogenase.
The cellobiose dehydrogenase may be obtained from microorganisms of any genus. For purposes of the present invention, the term “obtained from” as used herein in connection with a given source shall mean that the polypeptide encoded by a nucleotide sequence is produced by the source or by a strain in which the nucleotide sequence from the source has been inserted. In one aspect, the polypeptide obtained from a given source is secreted extracellularly.
The cellobiose dehydrogenase may be a bacterial polypeptide. For example, the polypeptide may be a gram positive bacterial polypeptide such as a Bacillus, Streptococcus, Streptomyces, Staphylococcus, Enterococcus, Lactobacillus, Lactococcus, Clostridium, Geobacillus, or Oceanobacillus cellobiose dehydrogenase, or a Gram negative bacterial polypeptide such as an E. coli, Pseudomonas, Salmonella, Campylobacter, Helicobacter, Flavobacterium, Fusobacterium, Ilyobacter, Neisseria, or Ureaplasma cellobiose dehydrogenase.
In one aspect, the polypeptide is a Bacillus alkalophilus, Bacillus amyloliquefaciens, Bacillus brevis, Bacillus circulans, Bacillus clausii, Bacillus coagulans, Bacillus firmus, Bacillus lautus, Bacillus lentus, Bacillus licheniformis, Bacillus megaterium, Bacillus pumilus, Bacillus stearothermophilus, Bacillus subtilis, or Bacillus thuringiensis cellobiose dehydrogenase.
In another aspect, the polypeptide is a Streptococcus equisimilis, Streptococcus pyogenes, Streptococcus uberis, or Streptococcus equi subsp. Zooepidemicus cellobiose dehydrogenase.
In another aspect, the polypeptide is a Streptomyces achromogenes, Streptomyces avermitilis, Streptomyces coelicolor, Streptomyces griseus, or Streptomyces lividans cellobiose dehydrogenase.
The cellobiose dehydrogenase may also be a fungal polypeptide, and more preferably a yeast polypeptide such as a Candida, Kluyveromyces, Pichia, Saccharomyces, Schizosaccharomyces, or Yarrowia cellobiose dehydrogenase; or more preferably a filamentous fungal polypeptide such as an Acremonium, Agaricus, Alternaria, Aspergillus, Aureobasidium, Botryospaeria, Ceriporiopsis, Chaetomidium, Chrysosporium, Claviceps, Cochliobolus, Coprinopsis, Coptotermes, Corynascus, Cryphonectria, Cryptococcus, Diplodia, Exidia, Filibasidium, Fusarium, Gibberella, Holomastigotoides, Humicola, Irpex, Lentinula, Leptospaeria, Magnaporthe, Melanocarpus, Meripilus, Mucor, Myceliophthora, Neocallimastix, Neurospora, Paecilomyces, Penicillium, Phanerochaete, Piromyces, Poitrasia, Pseudoplectania, Pseudotrichonympha, Rhizomucor, Schizophyllum, Scytalidium, Talaromyces, Thermoascus, Thielavia, Tolypocladium, Trichoderma, Trichophaea, Verticillium, Volvariella, or Xylaria cellobiose dehydrogenase.
In another aspect, the polypeptide is a Saccharomyces carlsbergensis, Saccharomyces cerevisiae, Saccharomyces diastaticus, Saccharomyces douglasii, Saccharomyces kluyveri, Saccharomyces norbensis, or Saccharomyces oviformis cellobiose dehydrogenase.
In another aspect, the polypeptide is an Acremonium cellulolyticus, Aspergillus aculeatus, Aspergillus awamori, Aspergillus fumigatus, Aspergillus foetidus, Aspergillus japonicus, Aspergillus nidulans, Aspergillus niger, Aspergillus oryzae, Chrysosporium keratinophilum, Chrysosporium lucknowense, Chrysosporium tropicum, Chrysosporium merdarium, Chrysosporium inops, Chrysosporium pannicola, Chrysosporium queenslandicum, Chrysosporium zonatum, Fusarium bactridioides, Fusarium cerealis, Fusarium crookwellense, Fusarium culmorum, Fusarium graminearum, Fusarium graminum, Fusarium heterosporum, Fusarium negundi, Fusarium oxysporum, Fusarium reticulatum, Fusarium roseum, Fusarium sambucinum, Fusarium sarcochroum, Fusarium sporotrichioides, Fusarium sulphureum, Fusarium torulosum, Fusarium trichothecioides, Fusarium venenatum, Humicola grisea, Humicola insolens, Humicola lanuginosa, Irpex lacteus, Mucor miehei, Myceliophthora thermophila, Neurospora crassa, Penicillium funiculosum, Penicillium purpurogenum, Phanerochaete chrysosporium, Thielavia achromatica, Thielavia albomyces, Thielavia albopilosa, Thielavia australeinsis, Thielavia fimeti, Thielavia microspora, Thielavia ovispora, Thielavia peruviana, Thielavia spededonium, Thielavia setosa, Thielavia subthermophila, Thielavia terrestris, Trichoderma harzianum, Trichoderma koningii, Trichoderma longibrachiatum, Trichoderma reesei, or Trichoderma viride cellobiose dehydrogenase.
Examples of other cellobiose dehydrogenases and their sources are listed in Table 1.







TABLE 1







Published microbial cellobiose dehydrogenase sequences










Accession 



Species
#
Literature Reference





Humicola insolens
Q9P8H5
Xu et al., 2001, Humicola insolens 




cellobiose dehydrogenase: cloning, redox 




chemistry, and “logic gate”-like dual 




functionality, Enz. Microb. Technol. 28: 




744-753


Irpex lacteus
Q6AW20
Nozaki et al., 1999, Cloning and expression 




of cellobiose dehydrogenase from Irpex 




lacteus. Submitted (AUG-2004) to the




EMBL/GenBank/DDBJ databases.


Pycnoporus
O74253
Moukha et al., 1999, Cloning and analysis 


cinnabarinus

of Pycnoporus cinnabarinus cellobiose




dehydrogenase, Gene 234: 23-33


Phanerochaete
Q01738
Li et al., 1996, Cloning of a cDNA 


chrysosporium

encoding cellobiose dehydrogenase, a 




hemoflavoenzyme from Phanerochaete 




chrysosporium, Appl. Environ. Microbiol. 




62: 1329-1335


Coniophora
Q6BDD5
Kajisa et al., 2004, Characterization and


puteana

molecular cloning of cellobiose 




dehydrogenase from the brown-rot fungus 




Coniophora puteana, Biosci. Bioeng. 98: 




57-63


Athelia rolfsii
Q7Z975
Zamocky et al., Phylogenetic analysis of




cellobiose dehydrogenases. Submitted 




(NOV-2002) to the EMBL/GenBank/DDBJ 




databases


Grifola
Q8J2T4
Yoshida et al., 2002, Molecular cloning 


frondosa

and characterization of a cDNA encoding 




cellobiose dehydrogenase from the wood-




rotting fungus Grifola frondosa, FEMS




Microbiol. Lett. 217: 225-230


Trametes
Q875J3
Stapleton et al., 2004, Molecular cloning of 


versicolor

the cellobiose dehydrogenase gene from 




Trametes versicolor and expression in 




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In another aspect, the cellobiose dehydrogenase is a Humicola insolens cellobiose dehydrogenase. In another aspect, the cellobiose dehydrogenase is a Humicola insolens DSM 1800 cellobiose dehydrogenase, e.g., the polypeptide comprising SEQ ID NO: 18 encoded by SEQ ID NO: 17, or a fragment thereof having cellobiose dehydrogenase activity (see U.S. Pat. No. 6,280,976).
In another aspect, the cellobiose dehydrogenase is a Myceliophthora thermophila cellobiose dehydrogenase. In another aspect, the cellobiose dehydrogenase is a Myceliophthora thermophila CBS 117.65 cellobiose dehydrogenase.
It will be understood that for the aforementioned species the invention encompasses both the perfect and imperfect states, and other taxonomic equivalents, e.g., anamorphs, regardless of the species name by which they are known. Those skilled in the art will readily recognize the identity of appropriate equivalents.
Strains of these species are readily accessible to the public in a number of culture collections, such as the American Type Culture Collection (ATCC), Deutsche Sammlung von Mikroorganismen and Zellkulturen GmbH (DSM), Centraalbureau Voor Schimmelcultures (CBS), and Agricultural Research Service Patent Culture Collection, Northern Regional Research Center (NRRL).
As described earlier, the techniques used to isolate or clone a polynucleotide encoding a polypeptide are known in the art and include isolation from genomic DNA, preparation from cDNA, or a combination thereof.
Enzyme Compositions
In the methods of the present invention, the enzyme composition may comprise any protein involved in the processing of a cellulose-containing material to glucose and/or cellobiose, or hemicellulose to xylose, mannose, galactose, and/or arabinose.
The enzyme composition preferably comprises enzymes having cellulolytic activity and/or xylan degrading activity. In one aspect, the enzyme composition comprises one or more (several) cellulolytic enzymes. In another aspect, the enzyme composition comprises one or more (several) xylan degrading enzymes. In another aspect, the enzyme composition comprises one or more (several) cellulolytic enzymes and one or more (several) xylan degrading enzymes.
The one or more (several) cellulolytic enzymes are preferably selected from the group consisting of an endoglucanase, a cellobiohydrolase, and a beta-glucosidase. The one or more (several) xylan degrading enzymes are preferably selected from the group consisting of a xylanase, an acetyxylan esterase, a feruloyl esterase, an arabinofuranosidase, a xylosidase, and a glucuronidase.
In another aspect, the enzyme composition further or even further comprises a polypeptide having cellulolytic enhancing activity (see, for example, WO 2005/074647, WO 2005/074656, and WO 2007/089290). In another aspect, the enzyme composition may further or even further comprise one or more (several) additional enzyme activities to improve the degradation of the cellulose-containing material. Preferred additional enzymes are hemicellulases (e.g., alpha-D-glucuronidases, alpha-L-arabinofuranosidases, endo-mannanases, beta-mannosidases, alpha-galactosidases, endo-alpha-L-arabinanases, beta-galactosidases), carbohydrate-esterases (e.g., acetyl-xylan esterases, acetyl-mannan esterases, ferulic acid esterases, coumaric acid esterases, glucuronoyl esterases), pectinases, proteases, ligninolytic enzymes (e.g., laccases, manganese peroxidases, lignin peroxidases, H2O2-producing enzymes, oxidoreductases), expansins, swollenins, or mixtures thereof. In the methods of the present invention, the additional enzyme(s) can be added prior to or during fermentation, e.g., during saccharification or during or after propagation of the fermenting microorganism(s).
One or more (several) components of the enzyme composition may be wild-type proteins, recombinant proteins, or a combination of wild-type proteins and recombinant proteins. For example, one or more (several) components may be native proteins of a cell, which is used as a host cell to express recombinantly one or more (several) other components of the enzyme composition. One or more (several) components of the enzyme composition may be produced as monocomponents, which are then combined to form the enzyme composition. The enzyme composition may be a combination of multicomponent and monocomponent protein preparations.
The enzymes used in the methods of the present invention may be in any form suitable for use in the processes described herein, such as, for example, a crude fermentation broth with or without cells removed, a cell lysate with or without cellular debris, a semi-purified or purified enzyme preparation, or a host cell as a source of the enzymes. The enzyme composition may be a dry powder or granulate, a non-dusting granulate, a liquid, a stabilized liquid, or a stabilized protected enzyme. Liquid enzyme preparations may, for instance, be stabilized by adding stabilizers such as a sugar, a sugar alcohol or another polyol, and/or lactic acid or another organic acid according to established processes.
A polypeptide having cellulolytic enzyme activity or xylan degrading activity may be a bacterial polypeptide. For example, the polypeptide may be a gram positive bacterial polypeptide such as a Bacillus, Streptococcus, Streptomyces, Staphylococcus, Enterococcus, Lactobacillus, Lactococcus, Clostridium, Geobacillus, or Oceanobacillus polypeptide having cellulolytic enzyme activity or xylan degrading activity, or a Gram negative bacterial polypeptide such as an E. coli, Pseudomonas, Salmonella, Campylobacter, Helicobacter, Flavobacterium, Fusobacterium, Ilyobacter, Neisseria, or Ureaplasma polypeptide having cellulolytic enzyme activity or xylan degrading activity.
In a preferred aspect, the polypeptide is a Bacillus alkalophilus, Bacillus amyloliquefaciens, Bacillus brevis, Bacillus circulans, Bacillus clausii, Bacillus coagulans, Bacillus firmus, Bacillus lautus, Bacillus lentus, Bacillus licheniformis, Bacillus megaterium, Bacillus pumilus, Bacillus stearothermophilus, Bacillus subtilis, or Bacillus thuringiensis polypeptide having cellulolytic enzyme activity or xylan degrading activity.
In another preferred aspect, the polypeptide is a Streptococcus equisimilis, Streptococcus pyogenes, Streptococcus uberis, or Streptococcus equi subsp. Zooepidemicus polypeptide having cellulolytic enzyme activity or xylan degrading activity.
In another preferred aspect, the polypeptide is a Streptomyces achromogenes, Streptomyces avermitilis, Streptomyces coelicolor, Streptomyces griseus, or Streptomyces lividans polypeptide having cellulolytic enzyme activity or xylan degrading activity.
The polypeptide having cellulolytic enzyme activity or xylan degrading activity may also be a fungal polypeptide, and more preferably a yeast polypeptide such as a Candida, Kluyveromyces, Pichia, Saccharomyces, Schizosaccharomyces, or Yarrowia polypeptide having cellulolytic enzyme activity or xylan degrading activity; or more preferably a filamentous fungal polypeptide such as an Acremonium, Agaricus, Alternaria, Aspergillus, Aureobasidium, Botryospaeria, Ceriporiopsis, Chaetomidium, Chrysosporium, Claviceps, Cochliobolus, Coprinopsis, Coptotermes, Corynascus, Cryphonectria, Cryptococcus, Diplodia, Exidia, Filibasidium, Fusarium, Gibberella, Holomastigotoides, Humicola, Irpex, Lentinula, Leptospaeria, Magnaporthe, Melanocarpus, Meripilus, Mucor, Myceliophthora, Neocallimastix, Neurospora, Paecilomyces, Penicillium, Phanerochaete, Piromyces, Poitrasia, Pseudoplectania, Pseudotrichonympha, Rhizomucor, Schizophyllum, Scytalidium, Talaromyces, Thermoascus, Thielavia, Tolypocladium, Trichoderma, Trichophaea, Verticillium, Volvariella, or Xylaria polypeptide having cellulolytic enzyme activity or xylan degrading activity.
In a preferred aspect, the polypeptide is a Saccharomyces carlsbergensis, Saccharomyces cerevisiae, Saccharomyces diastaticus, Saccharomyces douglasii, Saccharomyces kluyveri, Saccharomyces norbensis, or Saccharomyces oviformis polypeptide having cellulolytic enzyme activity or xylan degrading activity.
In another preferred aspect, the polypeptide is an Acremonium cellulolyticus, Aspergillus aculeatus, Aspergillus awamori, Aspergillus fumigatus, Aspergillus foetidus, Aspergillus japonicus, Aspergillus nidulans, Aspergillus niger, Aspergillus oryzae, Chrysosporium keratinophilum, Chrysosporium lucknowense, Chrysosporium tropicum, Chrysosporium merdarium, Chrysosporium inops, Chrysosporium pannicola, Chrysosporium queenslandicum, Chrysosporium zonatum, Fusarium bactridioides, Fusarium cerealis, Fusarium crookwellense, Fusarium culmorum, Fusarium graminearum, Fusarium graminum, Fusarium heterosporum, Fusarium negundi, Fusarium oxysporum, Fusarium reticulatum, Fusarium roseum, Fusarium sambucinum, Fusarium sarcochroum, Fusarium sporotrichioides, Fusarium sulphureum, Fusarium torulosum, Fusarium trichothecioides, Fusarium venenatum, Humicola grisea, Humicola insolens, Humicola lanuginosa, Irpex lacteus, Mucor miehei, Myceliophthora thermophila, Neurospora crassa, Penicillium funiculosum, Penicillium purpurogenum, Phanerochaete chrysosporium, Thielavia achromatica, Thielavia albomyces, Thielavia albopilosa, Thielavia australeinsis, Thielavia fimeti, Thielavia microspora, Thielavia ovispora, Thielavia peruviana, Thielavia spededonium, Thielavia setosa, Thielavia subthermophila, Thielavia terrestris, Trichoderma harzianum, Trichoderma koningii, Trichoderma longibrachiatum, Trichoderma reesei, Trichoderma viride, or Trichophaea saccata polypeptide having cellulolytic enzyme activity or xylan degrading activity.
Chemically modified or protein engineered mutants of polypeptides having cellulolytic enzyme activity or xylan degrading activity may also be used.
One or more (several) components of the enzyme composition may be a recombinant component, i.e., produced by cloning of a DNA sequence encoding the single component and subsequent cell transformed with the DNA sequence and expressed in a host (see, for example, WO 91/17243 and WO 91/17244). The host is preferably a heterologous host (enzyme is foreign to host), but the host may under certain conditions also be a homologous host (enzyme is native to host). Monocomponent cellulolytic proteins may also be prepared by purifying such a protein from a fermentation broth.
Examples of commercial cellulolytic protein preparations suitable for use in the present invention include, for example, CELLICTM Ctec (Novozymes A/S), CELLUCLASTTM (Novozymes A/S), NOVOZYMTM 188 (Novozymes A/S), CELLUZYMETM (Novozymes A/S), CEREFLOTM (Novozymes A/S), and ULTRAFLOTM (Novozymes A/S), ACCELERASETM (Genencor Int.), LAMINEXTM (Genencor Int.), SPEZYMETM CP (Genencor Int.), ROHAMENTTM 7069 W (Röhm GmbH), FIBREZYME® LDI (Dyadic International, Inc.), FIBREZYME® LBR (Dyadic International, Inc.), or VISCOSTAR® 150 L (Dyadic International, Inc.). The cellulase enzymes are added in amounts effective from about 0.001 to about 5.0 wt % of solids, more preferably from about 0.025 to about 4.0 wt % of solids, and most preferably from about 0.005 to about 2.0 wt % of solids. The cellulase enzymes are added in amounts effective from about 0.001 to about 5.0 wt % of solids, more preferably from about 0.025 to about 4.0 wt % of solids, and most preferably from about 0.005 to about 2.0 wt % of solids.
Examples of bacterial endoglucanases that can be used in the methods of the present invention, include, but are not limited to, an Acidothermus cellulolyticus endoglucanase (WO 91/05039; WO 93/15186; U.S. Pat. No. 5,275,944; WO 96/02551; U.S. Pat. No. 5,536,655, WO 00/70031, WO 05/093050); Thermobifida fusca endoglucanase III (WO 05/093050); and Thermobifida fusca endoglucanase V (WO 05/093050).
Examples of fungal endoglucanases that can be used in the methods of the present invention, include, but are not limited to, a Trichoderma reesei endoglucanase I (Penttila et al., 1986, Gene 45: 253-263; GENBANKTM accession no. M15665); Trichoderma reesei endoglucanase II (Saloheimo, et al., 1988, Gene 63:11-22; GENBANKTM accession no. M19373); Trichoderma reesei endoglucanase III (Okada et al., 1988, Appl. Environ. Microbiol. 64: 555-563; GENBANKTM accession no. AB003694); Trichoderma reesei endoglucanase IV (Saloheimo et al., 1997, Eur. J. Biochem. 249: 584-591; GENBANKTM accession no. Y11113); and Trichoderma reesei endoglucanase V (Saloheimo et al., 1994, Molecular Microbiology 13: 219-228; GENBANKTM accession no. Z33381); Aspergillus aculeatus endoglucanase (Ooi et al., 1990, Nucleic Acids Research 18: 5884); Aspergillus kawachii endoglucanase (Sakamoto et al., 1995, Current Genetics 27: 435-439); Erwinia carotovara endoglucanase (Saarilahti et al., 1990, Gene 90: 9-14); Fusarium oxysporum endoglucanase (GENBANKTM accession no. L29381); Humicola grisea var. thermoidea endoglucanase (GENBANKTM accession no. AB003107); Melanocarpus albomyces endoglucanase (GENBANKTM accession no. MAL515703); Neurospora crassa endoglucanase (GENBANKTM accession no. XM—324477); Humicola insolens endoglucanase V (SEQ ID NO: 20); Myceliophthora thermophila CBS 117.65 endoglucanase (SEQ ID NO: 22); basidiomycete CBS 495.95 endoglucanase (SEQ ID NO: 24); basidiomycete CBS 494.95 endoglucanase (SEQ ID NO: 26); Thielavia terrestris NRRL 8126 CEL6B endoglucanase (SEQ ID NO: 28); Thielavia terrestris NRRL 8126 CEL6C endoglucanase (SEQ ID NO: 30); Thielavia terrestris NRRL 8126 CEL7C endoglucanase (SEQ ID NO: 32); Thielavia terrestris NRRL 8126 CEL7E endoglucanase (SEQ ID NO: 34); Thielavia terrestris NRRL 8126 CEL7F endoglucanase (SEQ ID NO: 36); Cladorrhinum foecundissimum ATCC 62373 CEL7A endoglucanase (SEQ ID NO: 38); and Trichoderma reesei strain No. VTT-D-80133 endoglucanase (SEQ ID NO: 40; GENBANKTM accession no. M15665). The endoglucanases of SEQ ID NO: 20, SEQ ID NO: 22, SEQ ID NO: 24, SEQ ID NO: 26, SEQ ID NO: 28, SEQ ID NO: 30, SEQ ID NO: 32, SEQ ID NO: 34, SEQ ID NO: 36, SEQ ID NO: 38, and SEQ ID NO: 40 described above are encoded by the mature polypeptide coding sequence of SEQ ID NO: 19, SEQ ID NO: 21, SEQ ID NO: 23, SEQ ID NO: 25, SEQ ID NO: 27, SEQ ID NO: 29, SEQ ID NO: 31, SEQ ID NO: 33, SEQ ID NO: 35, SEQ ID NO: 37, SEQ ID NO: 39, respectively.
Examples of cellobiohydrolases useful in the methods of the present invention include, but are not limited to, Trichoderma reesei cellobiohydrolase I (SEQ ID NO: 42); Trichoderma reesei cellobiohydrolase II (SEQ ID NO: 44); Humicola insolens cellobiohydrolase I (SEQ ID NO: 46), Myceliophthora thermophila cellobiohydrolase II (SEQ ID NO: 48 and SEQ ID NO: 50), Thielavia terrestris cellobiohydrolase II (CEL6A) (SEQ ID NO: 52), Chaetomium thermophilum cellobiohydrolase I (SEQ ID NO: 54), and Chaetomium thermophilum cellobiohydrolase II (SEQ ID NO: 56). The cellobiohydrolases of SEQ ID NO: 40, SEQ ID NO: 42, SEQ ID NO: 44, SEQ ID NO: 46, SEQ ID NO: 48, SEQ ID NO: 50, SEQ ID NO: 52, and SEQ ID NO: 54 described above are encoded by the mature polypeptide coding sequence of SEQ ID NO: 41, SEQ ID NO: 43, SEQ ID NO: 45, SEQ ID NO: 47, SEQ ID NO: 49, SEQ ID NO: 51, SEQ ID NO: 53, and SEQ ID NO: 55, respectively.
Examples of beta-glucosidases useful in the methods of the present invention include, but are not limited to, Aspergillus oryzae beta-glucosidase (SEQ ID NO: 58); Aspergillus fumigatus beta-glucosidase (SEQ ID NO: 60); Penicillium brasilianum IBT 20888 beta-glucosidase (SEQ ID NO: 62); Aspergillus niger beta-glucosidase (SEQ ID NO: 64); and Aspergillus aculeatus beta-glucosidase (SEQ ID NO: 66). The beta-glucosidases of SEQ ID NO: 58, SEQ ID NO: 60, SEQ ID NO: 62, SEQ ID NO: 64, and SEQ ID NO: 66 described above are encoded by the mature polypeptide coding sequence of SEQ ID NO: 57, SEQ ID NO: 59, SEQ ID NO: 61, SEQ ID NO: 63, and SEQ ID NO: 65, respectively.
The Aspergillus oryzae polypeptide having beta-glucosidase activity can be obtained according to WO 2002/095014. The Aspergillus fumigatus polypeptide having beta-glucosidase activity can be obtained according to WO 2005/047499. The Penicillium brasilianum polypeptide having beta-glucosidase activity can be obtained according to WO 2007/019442. The Aspergillus niger polypeptide having beta-glucosidase activity can be obtained according to Dan et al., 2000, J. Biol. Chem. 275: 4973-4980. The Aspergillus aculeatus polypeptide having beta-glucosidase activity can be obtained according to Kawaguchi et al., 1996, Gene 173: 287-288.
The beta-glucosidase may be a fusion protein. In one aspect, the beta-glucosidase is the Aspergillus oryzae beta-glucosidase variant BG fusion protein of SEQ ID NO: 68 or the Aspergillus oryzae beta-glucosidase fusion protein of SEQ ID NO: 70. In another aspect, the Aspergillus oryzae beta-glucosidase variant BG fusion protein is encoded by the polynucleotide of SEQ ID NO: 67 or the Aspergillus oryzae beta-glucosidase fusion protein is encoded by the polynucleotide of SEQ ID NO: 69.
Other endoglucanases, cellobiohydrolases, and beta-glucosidases are disclosed in numerous Glycosyl Hydrolase families using the classification according to Henrissat B., 1991, A classification of glycosyl hydrolases based on amino-acid sequence similarities, Biochem. J. 280: 309-316, and Henrissat B., and Bairoch A., 1996, Updating the sequence-based classification of glycosyl hydrolases, Biochem. J. 316: 695-696.
Other cellulolytic enzymes that may be used in the present invention are described in EP 495,257, EP 531,315, EP 531,372, WO 89/09259, WO 94/07998, WO 95/24471, WO 96/11262, WO 96/29397, WO 96/034108, WO 97/14804, WO 98/08940, WO 98/012307, WO 98/13465, WO 98/015619, WO 98/015633, WO 98/028411, WO 99/06574, WO 99/10481, WO 99/025846, WO 99/025847, WO 99/031255, WO 2000/009707, WO 2002/050245, WO 2002/0076792, WO 2002/101078, WO 2003/027306, WO 2003/052054, WO 2003/052055, WO 2003/052056, WO 2003/052057, WO 2003/052118, WO 2004/016760, WO 2004/043980, WO 2004/048592, WO 2005/001065, WO 2005/028636, WO 2005/093050, WO 2005/093073, WO 2006/074005, WO 2006/117432, WO 2007/071818, WO 2007/071820, WO 2008/008070, WO 2008/008793, U.S. Pat. No. 4,435,307, U.S. Pat. No. 5,457,046, U.S. Pat. No. 5,648,263, U.S. Pat. No. 5,686,593, U.S. Pat. No. 5,691,178, U.S. Pat. No. 5,763,254, and U.S. Pat. No. 5,776,757.
Examples of commercial xylan degrading enzyme preparations suitable for use in the present invention include, for example, SHEARZYMETM (Novozymes A/S), CELLICTM Htec (Novozymes A/S), VISCOZYME® (Novozymes A/S), ULTRAFLO® (Novozymes A/S), PULPZYME® HC (Novozymes A/S), MULTIFECT® Xylanase (Genencor), ECOPULP® TX-200A (AB Enzymes), HSP 6000 Xylanase (DSM), DEPOLTM 333P (Biocatalysts Limit, Wales, UK), DEPOLTM 740 L. (Biocatalysts Limit, Wales, UK), and DEPOLTM 762P (Biocatalysts Limit, Wales, UK).
Examples of xylanases useful in the methods of the present invention include, but are not limited to, Aspergillus aculeatus xylanase (GeneSeqP:AAR63790; WO 94/21785), Aspergillus fumigatus xylanases (WO 2006/078256), and Thielavia terrestris NRRL 8126 xylanases (WO 2009/079210).
Examples of beta-xylosidases useful in the methods of the present invention include, but are not limited to, Trichoderma reesei beta-xylosidase (UniProtKB/TrEMBL accession number Q92458), Talaromyces emersonii (SwissProt accession number Q8×212), and Neurospora crassa (SwissProt accession number Q7SOW4).
Examples of acetylxylan esterases useful in the methods of the present invention include, but are not limited to, Hypocrea jecorina acetylxylan esterase (WO 2005/001036), Neurospora crassa acetylxylan esterase (UniProt accession number q7s259), Thielavia terrestris NRRL 8126 acetylxylan esterase (WO 2009/042846), Chaetomium globosum acetylxylan esterase (Uniprot accession number Q2GWX4), Chaetomium gracile acetylxylan esterase (GeneSeqP accession number AAB82124), Phaeosphaeria nodorum acetylxylan esterase (Uniprot accession number Q0UHJ1), and Humicola insolens DSM 1800 acetylxylan esterase (WO 2009/073709).
Examples of ferulic acid esterases useful in the methods of the present invention include, but are not limited to, Humicola insolens DSM 1800 feruloyl esterase (WO 2009/076122), Neurospora crassa feruloyl esterase (UniProt accession number Q9HGR3), and Neosartorya fischeri feruloyl esterase (UniProt Accession number A1D9T4).
Examples of arabinofuranosidases useful in the methods of the present invention include, but are not limited to, Humicola insolens DSM 1800 arabinofuranosidase (WO 2009/073383) and Aspergillus niger arabinofuranosidase (GeneSeqP accession number AAR94170).
Examples of alpha-glucuronidases useful in the methods of the present invention include, but are not limited to, Aspergillus clavatus alpha-glucuronidase (UniProt accession number alcc12), Trichoderma reesei alpha-glucuronidase (Uniprot accession number Q99024), Talaromyces emersonii alpha-glucuronidase (UniProt accession number Q8×211), Aspergillus niger alpha-glucuronidase (Uniprot accession number Q96WX9), Aspergillus terreus alpha-glucuronidase (SwissProt accession number Q0CJP9), and Aspergillus fumigatus alpha-glucuronidase (SwissProt accession number Q4WW45).
The enzymes and proteins used in the methods of the present invention may be produced by fermentation of the above-noted microbial strains on a nutrient medium containing suitable carbon and nitrogen sources and inorganic salts, using procedures known in the art (see, e.g., Bennett, J. W. and LaSure, L. (eds.), More Gene Manipulations in Fungi, Academic Press, CA, 1991). Suitable media are available from commercial suppliers or may be prepared according to published compositions (e.g., in catalogues of the American Type Culture Collection). Temperature ranges and other conditions suitable for growth and enzyme production are known in the art (see, e.g., Bailey, J. E., and 011 is, D. F., Biochemical Engineering Fundamentals, McGraw-Hill Book Company, NY, 1986).
The fermentation can be any method of cultivation of a cell resulting in the expression or isolation of an enzyme. Fermentation may, therefore, be understood as comprising shake flask cultivation, or small- or large-scale fermentation (including continuous, batch, fed-batch, or solid state fermentations) in laboratory or industrial fermentors performed in a suitable medium and under conditions allowing the enzyme to be expressed or isolated. The resulting enzymes produced by the methods described above may be recovered from the fermentation medium and purified by conventional procedures.
Nucleic Acid Constructs
Nucleic acid constructs comprising an isolated polynucleotide encoding a polypeptide of interest, e.g., polypeptide having cellulolytic enhancing activity or one or more (several) components of the enzyme composition, operably linked to one or more (several) control sequences may be constructed that direct the expression of the coding sequence in a suitable host cell under conditions compatible with the control sequences.
The isolated polynucleotide may be manipulated in a variety of ways to provide for expression of the polypeptide. Manipulation of the polynucleotide's sequence prior to its insertion into a vector may be desirable or necessary depending on the expression vector. The techniques for modifying polynucleotide sequences utilizing recombinant DNA methods are well known in the art.
The control sequence may be an appropriate promoter sequence, a nucleotide sequence that is recognized by a host cell for expression of a polynucleotide encoding a polypeptide of the present invention. The promoter sequence contains transcriptional control sequences that mediate the expression of the polypeptide. The promoter may be any nucleotide sequence that shows transcriptional activity in the host cell of choice including mutant, truncated, and hybrid promoters, and may be obtained from genes encoding extracellular or intracellular polypeptides either homologous or heterologous to the host cell.
Examples of suitable promoters for directing the transcription of the nucleic acid constructs of the present invention, especially in a bacterial host cell, are the promoters obtained from the E. coli lac operon, Streptomyces coelicolor agarase gene (dagA), Bacillus subtilis levansucrase gene (sacB), Bacillus licheniformis alpha-amylase gene (amyL), Bacillus stearothermophilus maltogenic amylase gene (amyM), Bacillus amyloliquefaciens alpha-amylase gene (amyQ), Bacillus licheniformis penicillinase gene (penP), Bacillus subtilis xylA and xylB genes, and prokaryotic beta-lactamase gene (Villa-Kamaroff et al., 1978, Proceedings of the National Academy of Sciences USA 75: 3727-3731), as well as the tac promoter (DeBoer et al., 1983, Proceedings of the National Academy of Sciences USA 80: 21-25). Further promoters are described in “Useful proteins from recombinant bacteria” in Scientific American, 1980, 242: 74-94; and in Sambrook et al., 1989, supra.
Examples of suitable promoters for directing the transcription of the nucleic acid constructs in a filamentous fungal host cell are promoters obtained from the genes for Aspergillus oryzae TAKA amylase, Rhizomucor miehei aspartic proteinase, Aspergillus niger neutral alpha-amylase, Aspergillus niger acid stable alpha-amylase, Aspergillus niger or Aspergillus awamori glucoamylase (glaA), Rhizomucor miehei lipase, Aspergillus oryzae alkaline protease, Aspergillus oryzae triose phosphate isomerase, Aspergillus nidulans acetamidase, Fusarium venenatum amyloglucosidase (WO 00/56900), Fusarium venenatum Dana (WO 00/56900), Fusarium venenatum Quinn (WO 00/56900), Fusarium oxysporum trypsin-like protease (WO 96/00787), Trichoderma reesei beta-glucosidase, Trichoderma reesei cellobiohydrolase I, Trichoderma reesei cellobiohydrolase II, Trichoderma reesei endoglucanase I, Trichoderma reesei endoglucanase II, Trichoderma reesei endoglucanase III, Trichoderma reesei endoglucanase IV, Trichoderma reesei endoglucanase V, Trichoderma reesei xylanase I, Trichoderma reesei xylanase II, Trichoderma reesei beta-xylosidase, as well as the NA2-tpi promoter (a modified promoter including a gene encoding a neutral alpha-amylase in Aspergilli in which the untranslated leader has been replaced by an untranslated leader from a gene encoding triose phosphate isomerase in Aspergilli; non-limiting examples include modified promoters including the gene encoding neutral alpha-amylase in Aspergillus niger in which the untranslated leader has been replaced by an untranslated leader from the gene encoding triose phosphate isomerase in Aspergillus nidulans or Aspergillus oryzae); and mutant, truncated, and hybrid promoters thereof.
In a yeast host, useful promoters are obtained from the genes for Saccharomyces cerevisiae enolase (ENO-1), Saccharomyces cerevisiae galactokinase (GAL1), Saccharomyces cerevisiae alcohol dehydrogenase/glyceraldehyde-3-phosphate dehydrogenase (ADH1, ADH2/GAP), Saccharomyces cerevisiae triose phosphate isomerase (TPI), Saccharomyces cerevisiae metallothionein (CUP1), and Saccharomyces cerevisiae 3-phosphoglycerate kinase. Other useful promoters for yeast host cells are described by Romanos et al., 1992, Yeast 8: 423-488.
The control sequence may also be a suitable transcription terminator sequence, a sequence recognized by a host cell to terminate transcription. The terminator sequence is operably linked to the 3′ terminus of the nucleotide sequence encoding the polypeptide. Any terminator that is functional in the host cell of choice may be used in the present invention.
Preferred terminators for filamentous fungal host cells are obtained from the genes for Aspergillus oryzae TAKA amylase, Aspergillus niger glucoamylase, Aspergillus nidulans anthranilate synthase, Aspergillus niger alpha-glucosidase, and Fusarium oxysporum trypsin-like protease.
Preferred terminators for yeast host cells are obtained from the genes for Saccharomyces cerevisiae enolase, Saccharomyces cerevisiae cytochrome C (CYC1), and Saccharomyces cerevisiae glyceraldehyde-3-phosphate dehydrogenase. Other useful terminators for yeast host cells are described by Romanos et al., 1992, supra.
The control sequence may also be a suitable leader sequence, a nontranslated region of an mRNA that is important for translation by the host cell. The leader sequence is operably linked to the 5′ terminus of the nucleotide sequence encoding the polypeptide. Any leader sequence that is functional in the host cell of choice may be used in the present invention.
Preferred leaders for filamentous fungal host cells are obtained from the genes for Aspergillus oryzae TAKA amylase and Aspergillus nidulans triose phosphate isomerase.
Suitable leaders for yeast host cells are obtained from the genes for Saccharomyces cerevisiae enolase (ENO-1), Saccharomyces cerevisiae 3-phosphoglycerate kinase, Saccharomyces cerevisiae alpha-factor, and Saccharomyces cerevisiae alcohol dehydrogenase/glyceraldehyde-3-phosphate dehydrogenase (ADH2/GAP).
The control sequence may also be a polyadenylation sequence, a sequence operably linked to the 3′ terminus of the nucleotide sequence and, when transcribed, is recognized by the host cell as a signal to add polyadenosine residues to transcribed mRNA. Any polyadenylation sequence that is functional in the host cell of choice may be used in the present invention.
Preferred polyadenylation sequences for filamentous fungal host cells are obtained from the genes for Aspergillus oryzae TAKA amylase, Aspergillus niger glucoamylase, Aspergillus nidulans anthranilate synthase, Fusarium oxysporum trypsin-like protease, and Aspergillus niger alpha-glucosidase.
Useful polyadenylation sequences for yeast host cells are described by Guo and Sherman, 1995, Molecular Cellular Biology 15: 5983-5990.
The control sequence may also be a signal peptide coding sequence that encodes a signal peptide linked to the amino terminus of a polypeptide and directs the encoded polypeptide into the cell's secretory pathway. The 5′ end of the coding sequence of the nucleotide sequence may inherently contain a signal peptide coding sequence naturally linked in translation reading frame with the segment of the coding sequence that encodes the secreted polypeptide. Alternatively, the 5′ end of the coding sequence may contain a signal peptide coding sequence that is foreign to the coding sequence. The foreign signal peptide coding sequence may be required where the coding sequence does not naturally contain a signal peptide coding sequence. Alternatively, the foreign signal peptide coding sequence may simply replace the natural signal peptide coding sequence in order to enhance secretion of the polypeptide. However, any signal peptide coding sequence that directs the expressed polypeptide into the secretory pathway of a host cell of choice, i.e., secreted into a culture medium, may be used in the present invention.
Effective signal peptide coding sequences for bacterial host cells are the signal peptide coding sequences obtained from the genes for Bacillus NCIB 11837 maltogenic amylase, Bacillus stearothermophilus alpha-amylase, Bacillus licheniformis subtilisin, Bacillus licheniformis beta-lactamase, Bacillus stearothermophilus neutral proteases (nprT, nprS, nprM), and Bacillus subtilis prsA. Further signal peptides are described by Simonen and Palva, 1993, Microbiological Reviews 57: 109-137.
Effective signal peptide coding sequences for filamentous fungal host cells are the signal peptide coding sequences obtained from the genes for Aspergillus oryzae TAKA amylase, Aspergillus niger neutral amylase, Aspergillus niger glucoamylase, Rhizomucor miehei aspartic proteinase, Humicola insolens cellulase, Humicola insolens endoglucanase V, and Humicola lanuginosa lipase.
Useful signal peptides for yeast host cells are obtained from the genes for Saccharomyces cerevisiae alpha-factor and Saccharomyces cerevisiae invertase. Other useful signal peptide coding sequences are described by Romanos et al., 1992, supra.
The control sequence may also be a propeptide coding sequence that encodes a propeptide positioned at the amino terminus of a polypeptide. The resultant polypeptide is known as a proenzyme or propolypeptide (or a zymogen in some cases). A propeptide is generally inactive and can be converted to a mature active polypeptide by catalytic or autocatalytic cleavage of the propeptide from the propolypeptide. The propeptide coding sequence may be obtained from the genes for Bacillus subtilis alkaline protease (aprE), Bacillus subtilis neutral protease (nprT), Saccharomyces cerevisiae alpha-factor, Rhizomucor miehei aspartic proteinase, and Myceliophthora thermophila laccase (WO 95/33836).
Where both signal peptide and propeptide sequences are present at the amino terminus of a polypeptide, the propeptide sequence is positioned next to the amino terminus of a polypeptide and the signal peptide sequence is positioned next to the amino terminus of the propeptide sequence.
It may also be desirable to add regulatory sequences that allow the regulation of the expression of the polypeptide relative to the growth of the host cell. Examples of regulatory systems are those that cause the expression of the gene to be turned on or off in response to a chemical or physical stimulus, including the presence of a regulatory compound. Regulatory systems in prokaryotic systems include the lac, tac, and trp operator systems. In yeast, the ADH2 system or GAL1 system may be used. In filamentous fungi, the TAKA alpha-amylase promoter, Aspergillus niger glucoamylase promoter, and Aspergillus oryzae glucoamylase promoter may be used as regulatory sequences. Other examples of regulatory sequences are those that allow for gene amplification. In eukaryotic systems, these regulatory sequences include the dihydrofolate reductase gene that is amplified in the presence of methotrexate, and the metallothionein genes that are amplified with heavy metals. In these cases, the nucleotide sequence encoding the polypeptide would be operably linked with the regulatory sequence.
Expression Vectors
Recombinant expression vectors comprising a polynucleotide encoding a polypeptide of interest, a promoter, and transcriptional and translational stop signals may be constructed for expression of the polypeptide in a suitable host cell. The various nucleic acids and control sequences described herein may be joined together to produce a recombinant expression vector that may include one or more (several) convenient restriction sites to allow for insertion or substitution of the nucleotide sequence encoding the polypeptide at such sites. Alternatively, a polynucleotide sequence may be expressed by inserting the nucleotide sequence or a nucleic acid construct comprising the sequence into an appropriate vector for expression. In creating the expression vector, the coding sequence is located in the vector so that the coding sequence is operably linked with the appropriate control sequences for expression.
The recombinant expression vector may be any vector (e.g., a plasmid or virus) that can be conveniently subjected to recombinant DNA procedures and can bring about expression of the nucleotide sequence. The choice of the vector will typically depend on the compatibility of the vector with the host cell into which the vector is to be introduced. The vectors may be linear or closed circular plasmids.
The vector may be an autonomously replicating vector, i.e., a vector that exists as an extrachromosomal entity, the replication of which is independent of chromosomal replication, e.g., a plasmid, an extrachromosomal element, a minichromosome, or an artificial chromosome. The vector may contain any means for assuring self-replication. Alternatively, the vector may be one that, when introduced into the host cell, is integrated into the genome and replicated together with the chromosome(s) into which it has been integrated. Furthermore, a single vector or plasmid or two or more vectors or plasmids that together contain the total DNA to be introduced into the genome of the host cell, or a transposon, may be used.
The vectors preferably contain one or more (several) selectable markers that permit easy selection of transformed, transfected, transduced, or the like cells. A selectable marker is a gene the product of which provides for biocide or viral resistance, resistance to heavy metals, prototrophy to auxotrophs, and the like.
Examples of bacterial selectable markers are the dal genes from Bacillus subtilis or Bacillus licheniformis, or markers that confer antibiotic resistance such as ampicillin, kanamycin, chloramphenicol, or tetracycline resistance. Suitable markers for yeast host cells are ADE2, HIS3, LEU2, LYS2, MET3, TRP1, and URA3. Selectable markers for use in a filamentous fungal host cell include, but are not limited to, amdS (acetamidase), argB (ornithine carbamoyltransferase), bar (phosphinothricin acetyltransferase), hph (hygromycin phosphotransferase), niaD (nitrate reductase), pyrG (orotidine-5′-phosphate decarboxylase), sC (sulfate adenyltransferase), and trpC (anthranilate synthase), as well as equivalents thereof. Preferred for use in an Aspergillus cell are the amdS and pyrG genes of Aspergillus nidulans or Aspergillus oryzae and the bar gene of Streptomyces hygroscopicus. 
The vectors preferably contain an element(s) that permits integration of the vector into the host cell's genome or autonomous replication of the vector in the cell independent of the genome.
For integration into the host cell genome, the vector may rely on the polynucleotide's sequence encoding the polypeptide or any other element of the vector for integration into the genome by homologous or nonhomologous recombination. Alternatively, the vector may contain additional nucleotide sequences for directing integration by homologous recombination into the genome of the host cell at a precise location(s) in the chromosome(s). To increase the likelihood of integration at a precise location, the integrational elements should preferably contain a sufficient number of nucleic acids, such as 100 to 10,000 base pairs, preferably 400 to 10,000 base pairs, and most preferably 800 to 10,000 base pairs, which have a high degree of identity to the corresponding target sequence to enhance the probability of homologous recombination. The integrational elements may be any sequence that is homologous with the target sequence in the genome of the host cell. Furthermore, the integrational elements may be non-encoding or encoding nucleotide sequences. On the other hand, the vector may be integrated into the genome of the host cell by non-homologous recombination.
For autonomous replication, the vector may further comprise an origin of replication enabling the vector to replicate autonomously in the host cell in question. The origin of replication may be any plasmid replicator mediating autonomous replication that functions in a cell. The term “origin of replication” or “plasmid replicator” is defined herein as a nucleotide sequence that enables a plasmid or vector to replicate in vivo.
Examples of bacterial origins of replication are the origins of replication of plasmids pBR322, pUC19, pACYC177, and pACYC184 permitting replication in E. coli, and pUB110, pE194, pTA1060, and pAMβ1 permitting replication in Bacillus. 
Examples of origins of replication for use in a yeast host cell are the 2 micron origin of replication, ARS1, ARS4, the combination of ARS1 and CEN3, and the combination of ARS4 and CEN6.
Examples of origins of replication useful in a filamentous fungal cell are AMA1 and ANS1 (Gems et al., 1991, Gene 98: 61-67; Cullen et al., 1987, Nucleic Acids Research 15: 9163-9175; WO 00/24883). Isolation of the AMA1 gene and construction of plasmids or vectors comprising the gene can be accomplished according to the methods disclosed in WO 00/24883.
More than one copy of a polynucleotide may be inserted into a host cell to increase production of the gene product. An increase in the copy number of the polynucleotide can be obtained by integrating at least one additional copy of the sequence into the host cell genome or by including an amplifiable selectable marker gene with the polynucleotide where cells containing amplified copies of the selectable marker gene, and thereby additional copies of the polynucleotide, can be selected for by cultivating the cells in the presence of the appropriate selectable agent.
The procedures used to ligate the elements described above to construct the recombinant expression vectors are well known to one skilled in the art (see, e.g., Sambrook et al., 1989, supra).
Host Cells
The nucleic acid constructs or expression vectors comprising an isolated polynucleotide encoding a polypeptide of interest may be introduced into recombinant host cells for the recombinant production of the polypeptides. A vector comprising a polynucleotide is introduced into a host cell so that the vector is maintained as a chromosomal integrant or as a self-replicating extra-chromosomal vector as described earlier. The term “host cell” encompasses any progeny of a parent cell that is not identical to the parent cell due to mutations that occur during replication. The choice of a host cell will to a large extent depend upon the gene encoding the polypeptide and its source.
The host cell may be any cell useful in the recombinant production of a polypeptide, e.g., a prokaryote or a eukaryote.
The prokaryotic host cell may be any Gram positive bacterium or a Gram negative bacterium. Gram positive bacteria include, but not limited to, Bacillus, Streptococcus, Streptomyces, Staphylococcus, Enterococcus, Lactobacillus, Lactococcus, Clostridium, Geobacillus, and Oceanobacillus. Gram negative bacteria include, but not limited to, E. coli, Pseudomonas, Salmonella, Campylobacter, Helicobacter, Flavobacterium, Fusobacterium, Ilyobacter, Neisseria, and Ureaplasma. 
The bacterial host cell may be any Bacillus cell. Bacillus cells include, but are not limited to, Bacillus alkalophilus, Bacillus amyloliquefaciens, Bacillus brevis, Bacillus circulans, Bacillus clausii, Bacillus coagulans, Bacillus firmus, Bacillus lautus, Bacillus lentus, Bacillus licheniformis, Bacillus megaterium, Bacillus pumilus, Bacillus stearothermophilus, Bacillus subtilis, and Bacillus thuringiensis cells.
In a preferred aspect, the bacterial host cell is a Bacillus amyloliquefaciens, Bacillus lentus, Bacillus licheniformis, Bacillus stearothermophilus or Bacillus subtilis cell. In a more preferred aspect, the bacterial host cell is a Bacillus amyloliquefaciens cell. In another more preferred aspect, the bacterial host cell is a Bacillus clausii cell. In another more preferred aspect, the bacterial host cell is a Bacillus licheniformis cell. In another more preferred aspect, the bacterial host cell is a Bacillus subtilis cell.
The bacterial host cell may also be any Streptococcus cell. Streptococcus cells include, but are not limited to, Streptococcus equisimilis, Streptococcus pyogenes, Streptococcus uberis, and Streptococcus equi subsp. Zooepidemicus cells.
In a preferred aspect, the bacterial host cell is a Streptococcus equisimilis cell. In another preferred aspect, the bacterial host cell is a Streptococcus pyogenes cell. In another preferred aspect, the bacterial host cell is a Streptococcus uberis cell. In another preferred aspect, the bacterial host cell is a Streptococcus equi subsp. Zooepidemicus cell.
The bacterial host cell may also be any Streptomyces cell. Streptomyces cells include, but are not limited to, Streptomyces achromogenes, Streptomyces avermitilis, Streptomyces coelicolor, Streptomyces griseus, and Streptomyces lividans cells.
In a preferred aspect, the bacterial host cell is a Streptomyces achromogenes cell. In another preferred aspect, the bacterial host cell is a Streptomyces avermitilis cell. In another preferred aspect, the bacterial host cell is a Streptomyces coelicolor cell. In another preferred aspect, the bacterial host cell is a Streptomyces griseus cell. In another preferred aspect, the bacterial host cell is a Streptomyces lividans cell.
The introduction of DNA into a Bacillus cell may, for instance, be effected by protoplast transformation (see, e.g., Chang and Cohen, 1979, Molecular General Genetics 168: 111-115), by using competent cells (see, e.g., Young and Spizizen, 1961, Journal of Bacteriology 81: 823-829, or Dubnau and Davidoff-Abelson, 1971, Journal of Molecular Biology 56: 209-221), by electroporation (see, e.g., Shigekawa and Dower, 1988, Biotechniques 6: 742-751), or by conjugation (see, e.g., Koehler and Thorne, 1987, Journal of Bacteriology 169: 5271-5278). The introduction of DNA into an E. coli cell may, for instance, be effected by protoplast transformation (see, e.g., Hanahan, 1983, J. Mol. Biol. 166: 557-580) or electroporation (see, e.g., Dower et al., 1988, Nucleic Acids Res. 16: 6127-6145). The introduction of DNA into a Streptomyces cell may, for instance, be effected by protoplast transformation and electroporation (see, e.g., Gong et al., 2004, Folia Microbiol. (Praha) 49: 399-405), by conjugation (see, e.g., Mazodier et al., 1989, J. Bacteriol. 171: 3583-3585), or by transduction (see, e.g., Burke et al., 2001, Proc. Natl. Acad. Sci. USA 98: 6289-6294). The introduction of DNA into a Pseudomonas cell may, for instance, be effected by electroporation (see, e.g., Choi et al., 2006, J. Microbiol. Methods 64: 391-397) or by conjugation (see, e.g., Pinedo and Smets, 2005, Appl. Environ. Microbiol. 71: 51-57). The introduction of DNA into a Streptococcus cell may, for instance, be effected by natural competence (see, e.g., Perry and Kuramitsu, 1981, Infect. Immun. 32: 1295-1297), by protoplast transformation (see, e.g., Catt and Jollick, 1991, Microbios. 68: 189-207, by electroporation (see, e.g., Buckley et al., 1999, Appl. Environ. Microbiol. 65: 3800-3804) or by conjugation (see, e.g., Clewell, 1981, Microbiol. Rev. 45: 409-436). However, any method known in the art for introducing DNA into a host cell can be used.
The host cell may also be a eukaryote, such as a mammalian, insect, plant, or fungal cell.
In a preferred aspect, the host cell is a fungal cell. “Fungi” as used herein includes the phyla Ascomycota, Basidiomycota, Chytridiomycota, and Zygomycota (as defined by Hawksworth et al., In, Ainsworth and Bisby's Dictionary of The Fungi, 8th edition, 1995, CAB International, University Press, Cambridge, UK) as well as the Oomycota (as cited in Hawksworth et al., 1995, supra, page 171) and all mitosporic fungi (Hawksworth et al., 1995, supra).
In a more preferred aspect, the fungal host cell is a yeast cell. “Yeast” as used herein includes ascosporogenous yeast (Endomycetales), basidiosporogenous yeast, and yeast belonging to the Fungi Imperfecti (Blastomycetes). Since the classification of yeast may change in the future, for the purposes of this invention, yeast shall be defined as described in Biology and Activities of Yeast (Skinner, F. A., Passmore, S. M., and Davenport, R. R., eds, Soc. App. Bacteriol. Symposium Series No. 9, 1980).
In an even more preferred aspect, the yeast host cell is a Candida, Hansenula, Kluyveromyces, Pichia, Saccharomyces, Schizosaccharomyces, or Yarrowia cell.
In a most preferred aspect, the yeast host cell is a Saccharomyces carlsbergensis, Saccharomyces cerevisiae, Saccharomyces diastaticus, Saccharomyces douglasii, Saccharomyces kluyveri, Saccharomyces norbensis, or Saccharomyces oviformis cell. In another most preferred aspect, the yeast host cell is a Kluyveromyces lactis cell. In another most preferred aspect, the yeast host cell is a Yarrowia lipolytica cell.
In another more preferred aspect, the fungal host cell is a filamentous fungal cell. “Filamentous fungi” include all filamentous forms of the subdivision Eumycota and Oomycota (as defined by Hawksworth et al., 1995, supra). The filamentous fungi are generally characterized by a mycelial wall composed of chitin, cellulose, glucan, chitosan, mannan, and other complex polysaccharides. Vegetative growth is by hyphal elongation and carbon catabolism is obligately aerobic. In contrast, vegetative growth by yeasts such as Saccharomyces cerevisiae is by budding of a unicellular thallus and carbon catabolism may be fermentative.
In an even more preferred aspect, the filamentous fungal host cell is an Acremonium, Aspergillus, Aureobasidium, Bjerkandera, Ceriporiopsis, Chrysosporium, Coprinus, Coriolus, Cryptococcus, Filibasidium, Fusarium, Humicola, Magnaporthe, Mucor, Myceliophthora, Neocallimastix, Neurospora, Paecilomyces, Penicillium, Phanerochaete, Phlebia, Piromyces, Pleurotus, Schizophyllum, Talaromyces, Thermoascus, Thielavia, Tolypocladium, Trametes, or Trichoderma cell.
In a most preferred aspect, the filamentous fungal host cell is an Aspergillus awamori, Aspergillus fumigatus, Aspergillus foetidus, Aspergillus japonicus, Aspergillus nidulans, Aspergillus niger or Aspergillus oryzae cell. In another most preferred aspect, the filamentous fungal host cell is a Fusarium bactridioides, Fusarium cerealis, Fusarium crookwellense, Fusarium culmorum, Fusarium graminearum, Fusarium graminum, Fusarium heterosporum, Fusarium negundi, Fusarium oxysporum, Fusarium reticulatum, Fusarium roseum, Fusarium sambucinum, Fusarium sarcochroum, Fusarium sporotrichioides, Fusarium sulphureum, Fusarium torulosum, Fusarium trichothecioides, or Fusarium venenatum cell. In another most preferred aspect, the filamentous fungal host cell is a Bjerkandera adusta, Ceriporiopsis aneirina, Ceriporiopsis aneirina, Ceriporiopsis caregiea, Ceriporiopsis gilvescens, Ceriporiopsis pannocinta, Ceriporiopsis rivulosa, Ceriporiopsis subrufa, Ceriporiopsis subvermispora, Chrysosporium keratinophilum, Chrysosporium lucknowense, Chrysosporium tropicum, Chrysosporium merdarium, Chrysosporium inops, Chrysosporium pannicola, Chrysosporium queenslandicum, Chrysosporium zonatum, Coprinus cinereus, Coriolus hirsutus, Humicola insolens, Humicola lanuginosa, Mucor miehei, Myceliophthora thermophila, Neurospora crassa, Penicillium purpurogenum, Phanerochaete chrysosporium, Phlebia radiata, Pleurotus eryngii, Thielavia terrestris, Trametes villosa, Trametes versicolor, Trichoderma harzianum, Trichoderma koningii, Trichoderma longibrachiatum, Trichoderma reesei, or Trichoderma viride cell.
Fungal cells may be transformed by a process involving protoplast formation, transformation of the protoplasts, and regeneration of the cell wall in a manner known per se. Suitable procedures for transformation of Aspergillus and Trichoderma host cells are described in EP 238 023 and Yelton et al., 1984, Proceedings of the National Academy of Sciences USA 81: 1470-1474. Suitable methods for transforming Fusarium species are described by Malardier et al., 1989, Gene 78: 147-156, and WO 96/00787. Yeast may be transformed using the procedures described by Becker and Guarente, In Abelson, J. N. and Simon, M. I., editors, Guide to Yeast Genetics and Molecular Biology, Methods in Enzymology, Volume 194, pp 182-187, Academic Press, Inc., New York; Ito et al., 1983, Journal of Bacteriology 153: 163; and Hinnen et al., 1978, Proceedings of the National Academy of Sciences USA 75: 1920.
Methods of Production
A polypeptide of interest, e.g., polypeptide having cellulolytic enhancing activity or one or more (several) cellulolytic enzymes, can be produced by (a) cultivating a cell, which in its wild-type form produces the polypeptide, under conditions conducive for production of the polypeptide; and (b) recovering the polypeptide.
The polypeptide of interest can also be produced by (a) cultivating a recombinant host cell, as described herein, under conditions conducive for production of the polypeptide; and (b) recovering the polypeptide.
In the production methods, the cells are cultivated in a nutrient medium suitable for production of the polypeptide using methods well known in the art. For example, the cell may be cultivated by shake flask cultivation, and small-scale or large-scale fermentation (including continuous, batch, fed-batch, or solid state fermentations) in laboratory or industrial fermentors performed in a suitable medium and under conditions allowing the polypeptide to be expressed and/or isolated. The cultivation takes place in a suitable nutrient medium comprising carbon and nitrogen sources and inorganic salts, using procedures known in the art. Suitable media are available from commercial suppliers or may be prepared according to published compositions (e.g., in catalogues of the American Type Culture Collection). If the polypeptide is secreted into the nutrient medium, the polypeptide can be recovered directly from the medium. If the polypeptide is not secreted into the medium, it can be recovered from cell lysates.
The polypeptides may be detected using methods known in the art that are specific for the polypeptides. These detection methods may include use of specific antibodies, formation of an enzyme product, or disappearance of an enzyme substrate. For example, an enzyme assay may be used to determine the activity of the polypeptide as described herein.
The resulting polypeptide may be recovered using methods known in the art. For example, the polypeptide may be recovered from the nutrient medium by conventional procedures including, but not limited to, centrifugation, filtration, extraction, spray-drying, evaporation, or precipitation.
The polypeptides may be purified by a variety of procedures known in the art including, but not limited to, chromatography (e.g., ion exchange, affinity, hydrophobic, chromatofocusing, and size exclusion), electrophoretic procedures (e.g., preparative isoelectric focusing), differential solubility (e.g., ammonium sulfate precipitation), SDS-PAGE, or extraction (see, e.g., Protein Purification, J.-C. Janson and Lars Ryden, editors, VCH Publishers, New York, 1989) to obtain substantially pure polypeptides.
The present invention is further described by the following examples that should not be construed as limiting the scope of the invention.
EXAMPLES
Example 1
Growth of Myceliophthora thermophila CBS 117.65
Two plugs from a PDA plate of Myceliophthora thermophila CBS 117.65 were inoculated into a 500 ml shake flask containing 100 ml of shake flask medium to obtain culture broth for the purification of a cellobiose dehydrogenase. PDA plates were composed of 39 g of potato dextrose agar and deionized water to 1 liter. The shake flask medium was composed of 15 g of glucose, 4 g of K2HPO4, 1 g of NaCl, 0.2 g of MgSO4.7H2O, 2 g of MES free acid, 1 g of Bacto Peptone, 5 g of yeast extract, 2.5 g of citric acid, 0.2 g of CaCl2.2H2O, 5 g of NH4NO3, 1 ml of trace elements solution, and deionized water to 1 liter. The trace elements solution was composed of 1.2 g of FeSO4.7H2O, 10 g of ZnSO4.7H2O, 0.7 g of MnSO4.H2O, 0.4 g of CuSO4.5H2O, 0.4 g of Na2B4O7.10H2O, 0.8 g of Na2MoO2.2H2O, and deionized water to 1 liter. The shake flask was incubated at 45° C. on an orbital shaker at 200 rpm for 48 hours. Fifty ml of the shake flask broth was used to inoculate a 2 liter fermentation vessel.
A total of 1.8 liters of the fermentation batch medium was added to a two liter glass jacketed fermentor (Applikon Biotechnology, Schiedam, Netherlands). Fermentation feed medium was dosed at a rate of 4 g/l/hour for a period of 72 hours. Fermentation batch medium was composed of 5 g of yeast extract, 176 g of powdered cellulose, 2 g of glucose, 1 g of NaCl, 1 g of Bacto Peptone, 4 g of K2HPO4, 0.2 g of CaCl2.2H2O, 0.2 g of MgSO4.7H2O, 2.5 g of citric acid, 5 g of NH4NO3, 1.8 ml of anti-foam, 1 ml of trace elements solution, and deionized water to 1 liter. The fermentation vessel was maintained at a temperature of 45° C. and pH was controlled using an Applikon 1030 control system (Applikon Biotechnology, Schiedam, Netherlands) to a set-point of 5.6+/−0.1. Air was added to the vessel at a rate of 1 vvm and the broth was agitated by Rushton impeller rotating at 1100 to 1300 rpm. At the end of the fermentation, whole broth was harvested from the vessel and centrifuged at 3000×g to remove the biomass.
Example 2
Purification of Myceliophthora thermophila CBS 117.65 Cellobiose Dehydrogenase
The Myceliophthora thermophila CBS 117.65 harvested broth described in Example 1 was centrifuged in 500 ml bottles at 13,000×g for 20 minutes at 4° C. and then sterile filtered using a 0.22 μm polyethersulfone membrane (Millipore, Bedford, Mass., USA). The filtered broth was concentrated and buffer exchanged with 20 mM Tris-HCl pH 8.5 using a tangential flow concentrator (Pall Filtron, Northborough, Mass., USA) equipped with a 10 kDa polyethersulfone membrane (Pall Filtron, Northborough, Mass., USA). To decrease the amount of pigment, the concentrate was applied to a 60 ml Q-SEPHAROSE BIG BEADTM column (GE Healthcare, Piscataway, N.J., USA) equilibrated with 20 mM Tris-HCl pH 8.5, and eluted stepwise with equilibration buffer containing 600 mM NaCl. Flow-through and eluate fractions were analyzed by SDS-PAGE using 8-16% CRITERIONTM SDS-PAGE gels (Bio-Rad Laboratories, Inc., Hercules, Calif., USA) and stained with GELCODETM Blue protein stain (Thermo Fisher Scientific, Waltham, Mass., USA). The eluate fraction contained cellobiose dehydrogenase (CBDH) as judged by the presence of a band corresponding to the apparent molecular weight of approximately 100 kDa by SDS-PAGE (Schou et al., 1998, Biochem. J. 330: 565-571).
The eluate fraction was concentrated using an AMICONTM ultrafiltration device (Millipore, Bedford, Mass., USA) equipped with a 10 kDa polyethersulfone membrane, and buffer-exchanged into 20 mM Tris-HCl pH 8.5 using a HIPREP® 26/10 desalting column (GE Heathcare, Piscataway, N.J., USA). The desalted material was loaded onto a MONO Q® column (HR 16/10, GE Healthcare, Piscataway, N.J., USA) equilibrated with 20 mM Tris-HCl pH 8.5. Bound proteins were eluted with a linear NaCl gradient from 0 to 500 mM (18 column volumes) in 20 mM Tris-HCl pH 8.5. Fractions were analyzed by SDS-PAGE as described above and the cellobiose dehydrogenase eluted at approximately 350-400 mM NaCl.
Fractions containing cellobiose dehydrogenase were pooled (60 ml) and mixed with an equal volume of 20 mM Tris-HCl pH 7.5 containing 3.4 M ammonium sulfate to yield a final concentration of 1.7 M ammonium sulfate. The sample was filtered (0.2 μM syringe filter, polyethersulfone membrane, Whatman, Maidstone, United Kingdom) to remove particulate matter prior to loading onto a Phenyl Superose column (HR 16/10, GE Healthcare, Piscataway, N.J., USA) equilibrated with 1.7 M ammonium sulfate in 20 mM Tris-HCl pH 7.5. Bound proteins were eluted with a decreasing 1.7→0 M ammonium sulfate gradient (12 column volumes) in 20 mM Tris-HCl pH 7.5. Fractions were analyzed by SDS-PAGE as described above and the cellobiose dehydrogenase eluted at approximately 800 mM ammonium sulfate. The cellobiose dehydrogenase fraction was >90% pure as judged by SDS-PAGE. CBDH activity was confirmed by a 2,6-dichlorophenolindophenol (DCIP) reduction assay in the presence of cellobiose, as described by Schou et al., 1998, supra.
Fractions containing cellobiose dehydrogenase were pooled, concentrated, and buffer exchanged into 20 mM Tris-HCl pH 7.5 by centrifugal concentration in a SORVALL® RT7 centrifuge (Thermo Fisher Scientific, Waltham, Mass., USA) using VIVASPINTM 20 centrifugal concentrators. (10 kDa polyethersulfone membrane; Sartorius, Göttingen, Germany) at 1877×g. Protein concentration was determined using a Microplate BCATM Protein Assay Kit (Thermo Fischer Scientific, Waltham, Mass., USA) in which bovine serum albumin was used as a protein standard.
Example 3
Pretreatment of Corn Stover
Corn stover was pretreated at the U.S. Department of Energy National Renewable Energy Laboratory (NREL) using dilute sulfuric acid. The following conditions were used for the pretreatment: 1.4 wt % sulfuric acid at 165° C. and 107 psi for 8 minutes. According to NREL, the water-insoluble solids in the pretreated corn stover (PCS) contained 56.5% cellulose, 4.6% hemicellulose and 28.4% lignin. Cellulose and hemicellulose were determined by a two-stage sulfuric acid hydrolysis with subsequent analysis of sugars by high performance liquid chromatography using NREL Standard Analytical Procedure #002. Lignin was determined gravimetrically after hydrolyzing the cellulose and hemicellulose fractions with sulfuric acid using NREL Standard Analytical Procedure #003. The PCS was washed with a large volume of DDI water on a glass filter.
Example 4
The Effect of Anaerobicity on Cellobiose Dehydrogenase-Inhibited PCS Hydrolysis
The effect of anaerobicity on hydrolysis of PCS was evaluated in the presence of Humicola insolens cellobiose dehydrogenase (CBDH) or Myceliophthora thermophila CBS 117.65 cellobiose dehydrogenase.
The hydrolysis of PCS was conducted using 125 ml Erlenmeyer flasks containing a total reaction mass of 50 g. The hydrolysis was performed with 16.5% total solids of unwashed, whole slurry PCS, equivalent to 47.85 mg of cellulose per ml, in 50 mM sodium acetate pH 5.0 buffer containing 1 mM manganese sulfate and a Trichoderma reesei cellulase composition (CELLUCLAST® supplemented with Aspergillus oryzae beta-glucosidase available from Novozymes A/S, Bagsværd, Denmark; the cellulase composition is designated herein in the Examples as “Trichoderma reesei cellulase composition”) at 4 mg per g of PCS. Cellobiose dehydrogenase was added at concentrations between 0 and 10% (w/w) of total protein. Flasks were incubated at 50° C. for 72-168 hours with shaking at 150 rpm. All experiments were performed in triplicate.
At various time points between 24 and 168 hours of incubation, 100 μl aliquots were removed and the extent of hydrolysis was assayed by high-performance liquid chromatography (HPLC) using the protocol described below.
To establish anaerobicity, buffer and PCS were added in 125 ml Erlenmeyer flasks and bubbled with gaseous nitrogen (N2) for approximately 5 minutes prior to enzyme addition in an environment bag (AtmosBag, Sigma Chemical Co., St. Louis, Mo., USA) under positive N2 pressure (ultrapure N2, Airgas). The Erlenmeyer flasks were then sealed with air-tight glass caps (Chemglass, Vineland, N.J., USA) using vacuum grease and secured with a wire cage. The reaction flasks were allowed to equilibrate at 50° C., returned to the N2 environment, vented to release gas pressure, and resealed. Hydrolysis was allowed to proceed at 50° C. for 72-168 hours. At various time points during the hydrolysis, the flasks were returned to the nitrogen environment and equilibrated at room temperature, and then 100 μl aliquots were removed and filtered. The soluble fractions were analyzed by HPLC. Suction was noted when caps were removed, indicating that an air-tight seal had been maintained over the course of the hydrolysis. In later experiments, anaerobic sensor strips (BD Bioscience, Sparks, Mo.) were affixed to the inside of the caps and confirmed that anaerobicity was generally maintained.
For HPLC analysis, samples were filtered with a 0.45 μm MULTISCREEN® 96-well filter plate (Millipore, Bedford, Mass., USA) and filtrates analyzed for sugar content as described below. When not used immediately, filtered aliquots were frozen at −20° C. The sugar concentrations of samples diluted in 0.005 M H2SO4 were measured using a 4.6×250 mm AMINEX® HPX-87H column (Bio-Rad Laboratories, Inc., Hercules, Calif., USA) by elution with 0.5% w/w benzoic acid-5 mM H2SO4 at a flow rate of 0.6 ml per minute at 65° C. for 11 minutes, and quantitation by integration of glucose and cellobiose signal from refractive index detection (CHEMSTATION®, AGILENT® 1100 HPLC, Agilent Technologies, Santa Clara, Calif., USA) calibrated by pure sugar samples. The resultant equivalents were used to calculate the percentage of cellulose conversion for each reaction. The extent of each hydrolysis was determined as the fraction of total cellulose converted to cellobiose+glucose, and were not corrected for soluble sugars present in PCS liquor.
All HPLC data processing was performed using Kaleidagraph software (Synergy software, Reading, Pa., USA). Measured sugar concentrations were adjusted for the appropriate dilution factor. Glucose and cellobiose were chromatographically separated and integrated and their respective concentrations determined independently. However, to calculate total conversion the glucose and cellobiose values were combined. Fractional hydrolysis is reported as the overall mass conversion of [glucose+cellobiose]/[total cellulose]. Triplicate data points were averaged and standard deviation was calculated.
The results (FIG. 1A) demonstrated that the Trichoderma reesei cellulase composition hydrolyzed PCS equally well whether under anaerobic or aerobic conditions. However, PCS hydrolysis in the presence of 5% Thermoascus aurantiacus GH61A polypeptide under anaerobic conditions was greater than that observed under aerobic conditions. The overall hydrolysis was improved approximately 3%.
The addition of Myceliopthora thermophila cellobiose dehydrogenase resulted in a 2% inhibition of PCS hydrolysis under aerobic conditions, and no inhibition under anaerobic conditions. Furthermore, the hydrolytic enhancement arising from GH61 addition was greater under anaerobic conditions than observed for aerobic hydrolysis.
FIG. 1B shows the kinetics of hydrolysis by 8 mg of the Trichoderma reesei cellulase composition per g cellulose plus 8 mg of cellobiose dehydrogenase per g cellulose demonstrating the higher extent of hydrolysis and the higher extent of CBDH inhibition. The data illustrated the reduction in cellobiose dehydrogenase inhibition by performing the hydrolysis under anaerobic conditions.
The addition of 0.4 mg of Humicola insolens cellobiose dehydrogenase per g cellulose to a hydrolysis reaction of 50 g of whole slurry pretreated corn stover by 4 mg of the Trichoderma reesei cellulase composition per g cellulose under anaerobic conditions was approximately 10% less inhibitory than a similar reaction performed under aerobic conditions (FIG. 1B).
Example 5
Effects of Anaerobicity on Hydrolysis of Pretreated Corn Stover (PCS)
Hydrolysis of PCS under anaerobic conditions was performed as described in Example 4 with the following changes. Saccharification reactions were bubbled with N2 for 5-minutes, adding the Trichoderma reesei cellulase composition and sealing the samples using vacuum-greased glass caps (Chemglass, Vineland, N.J., USA) and affixing wire caging to prevent loss of seal arising from gas expansion at higher temps, in a N2-inflated environment bag (AtmosBag, Sigma Chemical Co., St. Louis, Mo., USA) prior to incubation at 50° C. Fifty gram reactions were performed as described in Example 4 using various Trichoderma reesei cellulase composition concentrations as indicated. Reaction progress was assayed by removal of 200 μl aliquots for HPLC analysis from the Erlenmeyer flasks daily under N2 within the environment bag, and resealing. HPLC analysis was performed as described in Example 4.
The results (FIG. 2) demonstrated that PCS hydrolysis under anaerobic conditions yielded higher fractional hydrolysis at all enzyme concentrations and at all time points. The effect was most pronounced between 4 and 7 days of hydrolysis, and at the intermediate enzyme concentration of 8 mg per g cellulose. After 7 days of hydrolysis, the anaerobic enhancement over aerobic hydrolysis was 14-26%. The amount of enzyme required for 80% conversion of cellulose to glucose and cellobiose in 7 days was reduced from approximately 9 mg per g cellulose under aerobic conditions to approximately 5 mg per g cellulose under anaerobic conditions.
Example 6
Effect of Anaerobicity on Iron-Dependent Cellulase Inhibition
A series of 50 g scale hydrolyses of 25 g of AVICEL® (Sigma Chemical Co, St. Louis, Mo., USA) per liter by 0.25 g of the Trichoderma reesei cellulase composition per liter, with or without 0.025 g of Thermoascus aurantiacus GH61A polypeptide per liter and 1 mM FeSO4, in 50 mM sodium acetate pH 5.0 at 50° C., was performed under aerobic and anaerobic conditions as described in Example 5.
The results (FIG. 3) demonstrated that FeSO4 caused approximately a 30% decrease in the normal aerobic hydrolysis after one day, but not in the anaerobic hydrolysis. In the absence of FeSO4, slightly higher hydrolysis was also observed under anaerobic conditions.
The invention described and claimed herein is not to be limited in scope by the specific aspects herein disclosed, since these aspects are intended as illustrations of several aspects of the invention. Any equivalent aspects are intended to be within the scope of this invention.
Indeed, various modifications of the invention in addition to those shown and described herein will become apparent to those skilled in the art from the foregoing description. Such modifications are also intended to fall within the scope of the appended claims. In the case of conflict, the present disclosure including definitions will control.

## Claims

1. A method for pretreating a cellulosic material, comprising:
pretreating the cellulosic material under anaerobic conditions to produce a pretreated cellulosic material, wherein the pretreating of the cellulosic material is a chemical pretreatment and the anaerobic conditions are an oxygen level of no greater than 0.025 mM water-dissolved oxygen.

2. The method of claim 1, further comprising recovering the pretreated cellulosic material.

3. The method of claim 1, wherein the chemical pretreatment is selected from the group consisting of steam pretreatment with explosion, steam pretreatment without explosion, dilute acid pretreatment, hot liquid water pretreatment, alkaline pretreatment, lime pretreatment, wet explosion, ammonia fiber explosion, organosolv pretreatment, ammonia percolation pretreatment, ultrasound pretreatment, electroporation pretreatment, microwave pretreatment, supercritical CO2 pretreatment, supercritical H2O pretreatment, and gamma irradiation pretreatment.

4. The method of claim 1, wherein the anaerobic conditions are an oxygen level of no greater than 0.01 mM water-dissolved oxygen.

5. The method of claim 1, wherein the anaerobic conditions are an oxygen level of no greater than 0.002 mM water-dissolved oxygen.

6. The method of claim 1, wherein the anaerobic conditions during pretreatment increases the hydrolysis of the cellulosic material during saccharification compared to aerobic conditions during pretreatment.

7. The method of claim 1, wherein the anaerobic conditions are an oxygen level of no greater than 0.001 mM water-dissolved oxygen.

8. A method of obtaining a fermentable product further comprising:
(a) saccharifying the pretreated cellulosic material obtained by the method of claim 1 with an enzyme composition;
(b) fermenting the saccharified cellulosic material with one or more fermenting microorganisms to produce a fermentation product; and
(c) recovering the fermentation product from the fermentation.

9. The method of claim 8, wherein the enzyme composition comprises one or more cellulolytic enzymes, one or more xylan degrading enzymes, or one or more cellulolytic enzymes and one or more xylan degrading enzymes.

10. The method of claim 9, wherein the one or more cellulolytic enzymes are selected from the group consisting of an endoglucanase, a cellobiohydrolase, and a beta-glucosidase.

11. The method of claim 10, wherein the enzyme composition further comprises a polypeptide having cellulolytic enhancing activity.

12. The method of claim 9, wherein the one or more xylan degrading enzymes are selected from the group consisting of a xylanase, an acetyxylan esterase, a feruloyl esterase, an arabinofuranosidase, a xylosidase, a glucuronidase.

13. The method of claim 8, wherein step (a) and step (b) are performed simultaneously.

14. The method of claim 8, wherein the saccharification is performed under anaerobic conditions at an oxygen level of no greater than 0.025 mM water-dissolved oxygen.

15. The method of claim 14, wherein the saccharification is performed under anaerobic conditions at an oxygen level of no greater than 0.01 mM water-dissolved oxygen.

16. The method of claim 15, wherein the saccharification is performed under anaerobic conditions at an oxygen level of no greater than 0.002 mM water-dissolved oxygen.

17. The method of claim 8, wherein the fermentation product is an alcohol, an amino acid, a ketone, a gas, or an organic acid.

18. The method of claim 16, wherein the saccharification is performed under anaerobic conditions at an oxygen level of no greater than 0.001 mM water-dissolved oxygen.