VARIANTS OF GLUCOAMYLASE
Disclosed are combinatorial variants of a parent glucoamylase that have altered properties and are suitable such as for use within brewing and glucose syrup production. Also disclosed are DNA constructs encoding the variants and methods of producing the glucoamylase variants in host cells. Glucoamylase enzymes (glucan 1,4-α-glucohydrolases, EC 3.2.1.3) are starch hydrolyzing exo-acting carbohydrases, which catalyze the removal of successive glucose units from the non-reducing ends of starch or related oligo and polysaccharide molecules. Glucoamylases can hydrolyze both the linear and branched glucosidic linkages of starch (e.g., amylose and amylopectin). Glucoamylases are produced by numerous strains of bacteria, fungi, yeast and plants. Particularly interesting, and commercially important, glucoamylases are fungal enzymes that are extracellularly produced, for example from strains of Commercially, glucoamylases are very important enzymes and have been used in a wide variety of applications that require the hydrolysis of starch (e.g., for producing glucose and other monosaccharides from starch). Glucoamylases are used to produce high fructose corn sweeteners, which comprise over 50% of the sweetener market in the United States. In general, glucoamylases may be, and commonly are, used with alpha-amylases in starch hydrolyzing processes to hydrolyze starch to dextrins and then glucose. The glucose may then be converted to fructose by other enzymes (e.g., glucose isomerases); crystallized; or used in fermentations to produce numerous end products (e.g., ethanol, citric acid, lactic acid, succinate, ascorbic acid intermediates, glutamic acid, glycerol and 1,3-propanediol). Ethanol produced by using glucoamylases in the fermentation of starch and/or cellulose containing material may be used as a source of fuel or for alcoholic consumption. At the high solids concentrations used commercially for high glucose corn syrup (HGCS) and high fructose corn syrup (HFCS) production, glucoamylase synthesizes di-, tri-, and tetra-saccharides from glucose by condensation reactions. This occurs because of the slow hydrolysis of alpha-(1-6)-D-glucosidic bonds in starch and the formation of various accumulating condensation products, mainly isomaltose, from D-glucose. Accordingly, the glucose yield in many conventional processes does not exceed 95% of theoretical yield. The amount of syrups produced worldwide by this process is very large and even very small increases in the glucose yield pr ton of starch are commercially important. Glucoamylase is used in brewing mainly for production of low carb beer. In combination with other amylases (such as from the malt), glucoamylase gives a very extensive hydrolysis of starch, all the way down to glucose units. Glucose is readily converted to alcohol by yeast making it possible for the breweries to obtain a very high alcohol yield from fermentation and at the same time obtain a beer, which is very low in residual carbohydrate. The ferment is diluted down to the desired alcohol % with water, and the final beer is sold as “low carb”. Although glucoamylases have been used successfully in commercial applications for many years, a need still exists for new glucoamylases with altered properties, such as an improved specific activity, a reduced formation of condensation products such as isomaltose and increased thermostability. Citation or identification of any document in this application is not an admission that such document is available as prior art to the present invention. The glucoamylase variants and the use of glucoamylase variants for reducing the synthesis of condensation products during hydrolysis of starch are contemplated herein. These glucoamylase variants contain amino acid substitutions within the catalytic domains and/or the starch binding domain. The variants display altered properties, such as an altered specific activity, a reduced formation of condensation products such as isomaltose and/or altered thermostability. In one aspect, a glucoamylase variant is described herein comprising the following amino acid substitutions: a) 44R and 539R; or b) 44R, 61I and 539R, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase, wherein the glucoamylase variant has at least 80% sequence identity with SEQ ID NO: 1 or 2, or the parent glucoamylase. In a further aspect, the use is described of a glucoamylase variant for the preparation of an enzymatic composition. In a further aspect, the enzymatic composition comprises at least one additional enzyme selected among amylase, protease, pullulanase, isoamylase, cellulase, glucanase, xylanase, arabinofuranosidase, ferulic acid esterase, xylan acetyl esterase, phytase and a further glucoamylase such as for example an pullulanase and a alpha-amylase. In a further aspect, the use is described herein of a glucoamylase variant with a starch binding domain and a catalytic domain, said variant comprising two or more amino acid substitutions relative to the amino acid sequence of SEQ ID NO:2 or equivalent parent glucoamylase in interconnecting loop 2′, and/or in loop 1, and/or in helix 2, and/or in loop 11, and/or in helix 12 for reducing the synthesis of condensation products during hydrolysis of starch. In a further aspect, the use is described of a glucoamylase variant comprising two or more amino acid substitutions relative to interconnecting loop 2′ with the amino acid sequence from position 518 to position 543 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or loop 1 with the amino acid sequence from position 21 to position 51 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or helix 2 with the amino acid sequence from position 52 to position 68 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or loop 11 with the amino acid sequence from position 396 to position 420 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or helix 12 with the amino acid sequence from position 421 to position 434 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase for reducing the synthesis of condensation products during hydrolysis of starch. In a further aspect, the use is described of a glucoamylase variant comprising two or more amino acid substitutions relative to the amino acid sequence from position 518 to position 543 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or the amino acid sequence from position 21 to position 51 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or the amino acid sequence from position 52 to position 68 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or the amino acid sequence from position 396 to position 420 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or the amino acid sequence from position 421 to position 434 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase for reducing the synthesis of condensation products during hydrolysis of starch. In a further aspect, the use is described of a glucoamylase variant wherein said two or more amino acid substitutions are relative to the interconnecting loop 2′ with the amino acid sequence from position 518 to position 543 of SEQ ID NO:2, and/or loop 1 with the amino acid sequence from position 21 to position 51 of SEQ ID NO:2, and/or helix 2 with the amino acid sequence from position 52 to position 68 of SEQ ID NO:2, and/or loop 11 with the amino acid sequence from position 396 to position 420 of SEQ ID NO:2, and/or helix 12 with the amino acid sequence from position 421 to position 434 of SEQ ID NO:2. In a further aspect, the use of a glucoamylase variant which when in its crystal form has a crystal structure for which the atomic coordinates of the main chain atoms have a root-mean-square deviation from the atomic coordinates of the equivalent main chain atoms of TrGA (as defined in Table 20 in WO2009/067218) of less than 0.13 nm following alignment of equivalent main chain atoms, and which have a linker region, a starch binding domain and a catalytic domain, said variant comprising two or more amino acid substitutions relative to the amino acid sequence of the parent glucoamylase in interconnecting loop 2′ of the starch binding domain, and/or in loop 1, and/or in helix 2, and/or in loop 11, and/or in helix 12 of the catalytic domain for reducing the synthesis of condensation products during hydrolysis of starch. In one aspect, the glucoamylase variant comprises two or more amino acid substitutions, wherein an amino acid substitution is in position 539 and an amino acid substitution is in position 44, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase, and which sequence has at least 80% sequence identity to the parent glucoamylase, and wherein the amino acid substitution in position 44 is not 44C. The present disclosure further relates to a polynucleotide encoding a glucoamylase variant as described herein. One aspect, is a plasmid comprising a nucleic acid. Another aspect, is a vector comprising a polynucleotide as described, or capable of expressing a glucoamylase variant as described. Another aspect, is a host cell comprising, e.g. transformed with, a plasmid or a vector as described. Another aspect, is a host cell, which has stably integrated into the chromosome a nucleic acid sequence encoding the variant glucoamylase. Another aspect is a cell capable of expressing a glucoamylase variant as described. Another aspect is a method of expressing a glucoamylase variant, the method comprising obtaining a host cell or a cell and expressing the glucoamylase variant from the cell or host cell, and optionally purifying the glucoamylase variant. A further aspect of the disclosure is an enzymatic composition comprising at least one glucoamylase variant as described herein, and the use thereof. A further aspect of the disclosure is a method for converting starch or partially hydrolyzed starch into a syrup containing glucose, which process includes saccharifying a liquid starch solution in the presence of at least one glucoamylase variant or an enzymatic composition as described herein. A further aspect of the disclosure is the use of a glucoamylase variant as described herein in a starch conversion process, such as in a continuous starch conversion process, in a process for producing oligosaccharides, maltodextrins or glucose syrups and in a process for producing high fructose corn syrup. In a further aspect, the use of a glucoamylase variant as described herein in a alchohol fermentation process is provided. A further aspect of the disclosure is a method for producing a wort for brewing comprising forming a mash from a grist, and contacting the mash with a glucoamylase variant as described or an enzymatic composition as described. Yet a further aspect of the disclosure is a method for production of a beer which comprises: a) preparing a mash, b) filtering the mash to obtain a wort, and fermenting the wort to obtain a beer, wherein a glucoamylase variant as described is added to: step (a) and/or step (b) and/or step (c). Yet a further aspect of the disclosure is the use of a glucoamylase variant as described to enhance the production of fermentable sugars in either the mashing step or the fermentation step of a brewing process. Yet a further aspect of the disclosure is a beer, wherein the beer is produced by the steps of: a) preparing a mash, b) filtering the mash to obtain a wort, c) fermenting the wort to obtain a beer, and d) pasteurizing the beer, wherein a glucoamylase variant as described is added to: step (a) and/or step (b) and/or step (c). Accordingly, it is an object of the invention to not encompass within the invention any previously known product, process of making the product, or method of using the product such that Applicants reserve the right and hereby disclose a disclaimer of any previously known product, process, or method. It is further noted that the invention does not intend to encompass within the scope of the invention any product, process, or making of the product or method of using the product, which does not meet the written description and enablement requirements of the USPTO (35 U.S.C. §112, first paragraph) or the EPO (Article 83 of the EPC), such that Applicants reserve the right and hereby disclose a disclaimer of any previously described product, process of making the product, or method of using the product. It is noted that in this disclosure and particularly in the claims and/or embodiments, terms such as “comprises”, “comprised”, “comprising” and the like can have the meaning attributed to it in U.S. Patent law; e.g., they can mean “includes”, “included”, “including”, and the like; and that terms such as “consisting essentially of” and “consists essentially of” have the meaning ascribed to them in U.S. Patent law, e.g., they allow for elements not explicitly recited, but exclude elements that are found in the prior art or that affect a basic or novel characteristic of the invention. These and other embodiments are disclosed or are obvious from and encompassed by, the following Detailed Description. The following detailed description, given by way of example, but not intended to limit the invention solely to the specific embodiments described, may best be understood in conjunction with the accompanying drawings, in which: Glucoamylases are commercially important enzymes in a wide variety of applications that require the hydrolysis of starch. The applicants have found that by introducing certain alterations in positions within specific regions of the amino acid sequence of a parent glucoamylase the rate of forming alpha-(1-6) bonds is reduced, and/or the formation of condensation products such as isomaltose is reduced. A reduction of the rate that glucoamylase forms alpha-(1-6) bonds relative to the rate it cleaves alpha-(1-4) bonds has practical implications. The present inventors have provided a number of variants of a parent glucoamylase, which variants in some embodiments show a reduced condensation and/or a reduced ratio between isomaltose synthesis and starch hydrolysis activity (IS/SH ratio) as compared to the parent glucoamylase. In some embodiments using a glucoamylase variant as described herein in a saccharification process produces a syrup with high glucose percentage. In some embodiments using a glucoamylase variant as described herein results in an enhanced production of fermentable sugars in a mashing and/or fermentation step of a brewing step. In some embodiments using a glucoamylase variant as described herein results in an enhanced real degree of fermentation. These altered properties are obtained by mutating e.g. substituting selected positions in a parent glucoamylase. This will be described in more detail below. Accordingly, in a further aspect, the use is described of a glucoamylase variant comprising two or more amino acid substitutions relative to interconnecting loop 2′ with the amino acid sequence from position 518 to position 543 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or loop 1 with the amino acid sequence from position 21 to position 51 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or helix 2 with the amino acid sequence from position 52 to position 68 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or loop 11 with the amino acid sequence from position 396 to position 420 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or helix 12 with the amino acid sequence from position 421 to position 434 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase for reducing the synthesis of condensation products during hydrolysis of starch. In a further aspect, the use is described of a glucoamylase variant comprising two or more amino acid substitutions relative to the amino acid sequence from position 518 to position 543 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or the amino acid sequence from position 21 to position 51 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or the amino acid sequence from position 52 to position 68 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or the amino acid sequence from position 396 to position 420 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or the amino acid sequence from position 421 to position 434 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase for reducing the synthesis of condensation products during hydrolysis of starch. Accordingly, in a further aspect, the use of a glucoamylase variant is described, which glucoamylase variant when in its crystal form has a crystal structure for which the atomic coordinates of the main chain atoms have a root-mean-square deviation from the atomic coordinates of the equivalent main chain atoms of TrGA (as defined in Table 20 in WO2009/067218) of less than 0.13 nm following alignment of equivalent main chain atoms, and which have a linker region, a starch binding domain and a catalytic domain, said variant comprising two or more amino acid substitutions relative to the amino acid sequence of the parent glucoamylase in interconnecting loop 2′ of the starch binding domain, and/or in loop 1, and/or in helix 2, and/or in loop 11, and/or in helix 12 of the catalytic domain for reducing the synthesis of condensation products during hydrolysis of starch. In a further aspect, the root-mean-square deviation from the atomic coordinates of the equivalent main chain atoms of TrGA (as defined in Table 20 in WO2009/067218) is less than 0.12 nm, such as less than 0.11 or such as less than 0.10. In one aspect, the use is described herein of a glucoamylase variant with a starch binding domain and a catalytic domain, said variant comprising two or more amino acid substitutions relative to the amino acid sequence of SEQ ID NO:2 or equivalent parent glucoamylase in interconnecting loop 2′, and/or in loop 1, and/or in helix 2, and/or in loop 11, and/or in helix 12 for reducing the synthesis of condensation products during hydrolysis of starch. In a further aspect, the use is described of a glucoamylase variant wherein said two or more amino acid substitutions are relative to the interconnecting loop 2′ with the amino acid sequence from position 518 to position 543 of SEQ ID NO:2 or equivalent sequence of residues in parent glucoamylase, and/or loop 1 with the amino acid sequence from position 21 to position 51 of SEQ ID NO:2 or equivalent sequence of residues in parent glucoamylase, and/or helix 2 with the amino acid sequence from position 52 to position 68 of SEQ ID NO:2 or equivalent sequence of residues in parent glucoamylase, and/or loop 11 with the amino acid sequence from position 396 to position 420 of SEQ ID NO:2 or equivalent sequence of residues in parent glucoamylase, and/or helix 12 with the amino acid sequence from position 421 to position 434 of SEQ ID NO:2 or equivalent sequence of residues in parent glucoamylase. In a further aspect, the use is described of a glucoamylase variant wherein said two or more amino acid substitutions are relative to the interconnecting loop 2′ with the amino acid sequence from position 518 to position 543 of SEQ ID NO:2, and/or loop 1 with the amino acid sequence from position 21 to position 51 of SEQ ID NO:2, and/or helix 2 with the amino acid sequence from position 52 to position 68 of SEQ ID NO:2, and/or loop 11 with the amino acid sequence from position 396 to position 420 of SEQ ID NO:2, and/or helix 12 with the amino acid sequence from position 421 to position 434 of SEQ ID NO:2. In a further aspect, the two or more amino acid substitutions are at least one such as one, two or three amino acid substitution in the interconnecting loop 2′ and at least one such as one, two, three, four, five or six amino acid substitution in loop 1 and/or helix 2 and/or loop 11 and/or helix 12. In a further aspect, the two or more amino acid substitutions are one, two, three or four amino acid substitutions in the interconnecting loop 2′ and one, two, three or four amino acid substitutions in loop 1 and/or helix 2 and/or loop 11 and/or helix 12. In a further aspect, there are one, two, three or four amino acid substitutions in the interconnecting loop 2′. In a further aspect, there are one, two, three or four amino acid substitutions in loop 1. In a further aspect, there are one, two, three or four amino acid substitutions in helix 2. In a further aspect, there are one, two, three or four amino acid substitutions in loop 11. In a further aspect, there are one, two, three or four amino acid substitutions in helix 12. In a further aspect, the two or more amino acid substitutions are at least one amino acid substitution in interconnecting loop 2′ and at least one amino acid substitution in loop 1. In a further aspect, the two or more amino acid substitutions are at least one amino acid substitution in interconnecting loop 2′ and at least one amino acid substitution in helix 2. In a further aspect, the two or more amino acid substitutions are at least one amino acid substitution in interconnecting loop 2′ and at least one amino acid substitution in loop 11. In a further aspect, the two or more amino acid substitutions are at least one amino acid substitution in interconnecting loop 2′ and at least one amino acid substitution in helix 12. In a further aspect, the two or more amino acid substitutions are at least one amino acid substitution in interconnecting loop 2′ and at least one amino acid substitution in loop 1 and at least one amino acid substitution in helix 2. In a further aspect, the glucoamylase variant has at least one amino acid substitution within position 520-543, 530-543, or 534-543 of interconnecting loop 2′, the positions corresponding to the respective position in SEQ ID NO:2 or equivalent positions in a parent glucoamylase. In a further aspect, the glucoamylase variant has at least one amino acid substitution within the amino acid sequence of position 30-50, 35-48, or 40-46 of loop 1, the positions corresponding to the respective position in SEQ ID NO:2 or equivalent positions in a parent glucoamylase. In a further aspect, the glucoamylase variant has at least one amino acid substitution within the amino acid sequence of position 50-66, 55-64, or 58-63 of helix 2, the positions corresponding to the respective position in SEQ ID NO:2 or equivalent positions in a parent glucoamylase. In a further aspect, the glucoamylase variant has at least one amino acid substitution within the amino acid sequence of position 405-420, 410-420, or 415-420 of loop 11, the positions corresponding to the respective position in SEQ ID NO:2 or equivalent positions in a parent glucoamylase. In a further aspect, the glucoamylase variant has at least one amino acid substitution within the amino acid sequence of position 421-434, 425-434, or 428-434 of helix 12, the positions corresponding to the respective position in SEQ ID NO:2 or equivalent positions in a parent glucoamylase. In a further aspect, the glucoamylase variant has at least 80%, 85%, 90%, 95%, 98%, or 99.5% sequence identity to the parent glucoamylase, such as at least 80%, 85%, 90%, 95%, 98%, or 99.5% sequence identity to SEQ ID NO: 1, 2, 3, 5, 6, 7, 8, or 9. In one aspect, the glucoamylase variant has at least 80%, 85%, 90%, 95%, 98%, or 99.5% sequence identity to SEQ ID NO:2. In a further aspect, the parent glucoamylase or the glucoamylase variant has a starch binding domain that has at least 96%, 97%, 98%, 99%, or 99.5% sequence identity with the starch binding domain of SEQ ID NO: 1, 2, 11, 385, 386, 387, 388, 389, or 390. In a further aspect, the parent glucoamylase or the glucoamylase variant has a catalytic domain that has at least 80%, 85%, 90%, 95%, or 99.5% sequence identity with the catalytic domain of SEQ ID NO: 1, 2, 3, 5, 6, 7, 8, or 9. In one aspect, the glucoamylase variant has an amino acid substitution in position 539 and one or more amino acid substitutions in a position selected from position 44, 61, 417 and 431, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In one aspect, the glucoamylase variant has an amino acid substitution in position 539 and a) an amino acid substitution in position 44 and/or b) amino acid substitutions in both positions 417 and 431, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In one aspect, the glucoamylase variant has an amino acid substitution in position 539 and an amino acid substitution in position 44, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In one aspect, the glucoamylase variant has an amino acid substitution in position 539 and amino acid substitutions in positions 417 and 431, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In one aspect, the glucoamylase variant has an amino acid substitution in position 539 and amino acid substitutions in positions 44 and 61, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In one aspect, the glucoamylase variant has an amino acid substitution in position 43, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In one aspect, the glucoamylase variant has an amino acid substitution in position 61, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In one aspect, the amino acid substitution in position 539 is A539R, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In one aspect, the amino acid substitution in position 44 is 44R, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In one aspect, the amino acid substitution in position 417 is 417R/V, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In one aspect, the amino acid substitution in position 417 is 417R, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In one aspect, the amino acid substitution in position 417 is 417V, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In one aspect, the amino acid substitution in position 431 is 431L, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In one aspect, the amino acid substitution in position 43 is 43R, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In one aspect, the amino acid substitution in position 61 is 61I, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In one aspect, the condensation product is isomaltose. In one aspect, the hydrolysis of starch is in a brewing process. In for example brewing, the formation of isomaltose is undesired because it can not be converted into alcohol during fermentation. Beer is traditionally referred to as an alcoholic beverage derived from malt, such as malt derived from barley, and optionally adjuncts, such as cereal grains, and flavoured with hops. Beer can be made from a variety of grains by essentially the same process. All grain starches are glucose homopolymers in which the glucose residues are linked by either alpha-1,4- or alpha-1,6-bonds, with the former predominating. The process of making fermented malt beverages is commonly referred to as brewing. The principal raw materials used in making these beverages are water, hops and malt. In addition, adjuncts such as common corn grits, refined corn grits, brewer's milled yeast, rice, sorghum, refined corn starch, barley, barley starch, dehusked barley, wheat, wheat starch, torrified cereal, cereal flakes, rye, oats, potato, tapioca, and syrups, such as corn syrup, sugar cane syrup, inverted sugar syrup, barley and/or wheat syrups, and the like may be used as a source of starch. The starch will eventually be converted into dextrins and fermentable sugars. For a number of reasons, the malt, which is produced principally from selected varieties of barley, is believed to have the greatest effect on the overall character and quality of the beer. First, the malt is the primary flavouring agent in beer. Second, the malt provides the major portion of the fermentable sugar. Third, the malt provides the proteins, which will contribute to the body and foam character of the beer. Fourth, the malt provides the necessary enzymatic activity during mashing. Hops also contribute significantly to beer quality, including flavouring. In particular, hops (or hops constituents) add desirable bittering substances to the beer. In addition, the hops act as protein precipitants, establish preservative agents and aid in foam formation and stabilization. The process for making beer is well known in the art, but briefly, it involves five steps: (a) mashing and/or adjunct cooking (b) wort separation and extraction (c) boiling and hopping of wort (d) cooling, fermentation and storage, and (e) maturation, processing and packaging. Typically, in the first step, milled or crushed malt is mixed with water and held for a period of time under controlled temperatures to permit the enzymes present in the malt to convert the starch present in the malt into fermentable sugars. In the second step, the mash is transferred to a “Iauter tun” or mash filter where the liquid is separated from the grain residue. This sweet liquid is called “wort” and the left over grain residue is called “spent grain”. The mash is typically subjected to an extraction, which involves adding water to the mash in order to recover the residual soluble extract from the spent grain. In the third step, the wort is boiled vigorously. This sterilizes the wort and helps to develop the colour, flavour and odour and inactivates enzyme activities. Hops are added at some point during the boiling. In the fourth step, the wort is cooled and transferred to a fermentor, which either contains the yeast or to which yeast is added. The yeast converts the sugars by fermentation into alcohol and carbon dioxide gas; at the end of fermentation the fermentor is chilled or the fermentor may be chilled to stop fermentation. The yeast flocculates and is removed. In the last step, the beer is cooled and stored for a period of time, during which the beer clarifies and its flavour develops, and any material that might impair the appearance, flavour and shelf life of the beer settles out. Prior to packaging, the beer is carbonated and, optionally, filtered and pasteurized. After fermentation, a beverage is obtained which usually contains from about 2% to about 10% alcohol by weight. The non-fermentable carbohydrates are not converted during fermentation and form the majority of the dissolved solids in the final beer. This residue remains because of the inability of malt amylases to hydrolyze the alpha-1,6-linkages of the starch. The non-fermentable carbohydrates contribute about 50 calories per 12 ounces of beer. Further information on conventional brewing processes, as well as definitions for terms used in the field of brewing technology to be applied for the present invention, may be found in “Technology Brewing and Malting” by Wolfgang Kunze of the Research and Teaching Institute of Brewing, Berlin (VLB), 2nd revised Edition 1999, ISBN 3-921690-39-0 or 3rd edition (2004): ISBN 3-921690-49-8. Recently, there has been a widespread popularization of brewed beverages called light beers, reduced calorie beers or low calorie beers, particularly in the U.S. market. As defined in the U.S., these beers have approximately 30% fewer calories than a manufacturer's “normal” beer. As used herein, the term “light beers, reduced calorie beers or low calorie beers”, refers to the recent, widespread popularization of brewed beverages, particularly in the U.S. market. As defined in the U.S., these highly attenuated beers have approximately 30% fewer calories than a manufacturer's “normal beer”. Further information on conventional brewing processes may be found in “Technology Brewing and Malting” by Wolfgang Kunze of the Research and Teaching Institute of Brewing, Berlin (VLB), 3rd completely updated edition, 2004, ISBN 3-921690-49-8.” Disclosed herein is the use of a glucoamylase variant as described herein, wherein the production of fermentable sugar(s) is enhanced as compared to the parent glucoamylase, such as TrGA. Further disclosed herein is the use of a glucoamylase variant as described herein, wherein the production of fermentable sugars is enhanced in a mashing step of the brewing process as compared to the parent glucoamylase, such as TrGA. Disclosed herein is the use of a glucoamylase variant as described herein, wherein the production of fermentable sugars is enhanced in a fermentation step of a brewing process as compared to the parent glucoamylase, such as TrGA. Disclosed herein is the use of a glucoamylase variant as described herein, wherein the fermentable sugar is glucose. A glucoamylase that can produce glucose with a significantly reduced amount of by-products would be of great commercial interest, e.g. in production of glucose syrup or in brewing. Further disclosed herein is the use of a glucoamylase variant as described herein, wherein the hydrolysis of starch is in a process for producing glucose syrup. In one aspect, the glucoamylase exhibit a reduced ratio between isomaltose synthesis (IS) and starch hydrolysis activity (SH) as compared to the parent glucoamylase, such as TrGA. In one aspect, the glucoamylase exhibit a reduced starch hydrolysis activity, which is not more than 5%, not more than 10% or not more than 15% reduced as compared to the parent glucoamylase, such as TrGA. In one aspect, the glucoamylase exhibit an enhanced real degree of fermentation as compared to the parent glucoamylase such as TrGA. In one aspect, the glucoamylase forms a lower amount of condensation products than the amount of condensation products formed by the glucoamylase Glucoamylase variants described herein contain amino acid substitutions within the catalytic domain and/or the starch binding domain. The variants may display altered properties such as improved thermostability, altered formation of condensation products such as isomaltose and/or an enhanced real degree of fermentation and/or a reduced ratio between isomaltose synthesis (IS) and starch hydrolysis activity (SH) and/or specific activity. The variants with reduced formation of condensation products such as isomaltose may significantly improve the ability to make desired products in the brewing industry, for example. Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this disclosure belongs. Singleton et al., As used herein, the term “glucoamylase (EC 3.2.1.3)” refers to an enzyme that catalyzes the release of D-glucose from the non-reducing ends of starch and related oligo- and polysaccharides. The term “parent” or “parent sequence” refers to a sequence that is native or naturally occurring in a host cell. Parent glucoamylases include, but are not limited to, the glucoamylase sequences set forth in SEQ ID NOs: 1, 2, 3, 5, 6, 7, 8, and 9, and glucoamylases with at least 80% amino acid sequence identity to SEQ ID NO: 2. As used herein, an “equivalent position” means a position that is common to two parent sequences that is based on an alignment of the amino acid sequence of the parent glucoamylase in question as well as alignment of the three-dimensional structure of the parent glucoamylase in question with the TrGA reference glucoamylase amino acid sequence (SEQ ID NO: 2) and three-dimensional structure. Thus either sequence alignment or structural alignment may be used to determine equivalence. The term “TrGA” refers to a parent The phrase “mature form of a protein or polypeptide” refers to the final functional form of the protein or polypeptide. A mature form of a glucoamylase may lack a signal peptide, for example. To exemplify, a mature form of the TrGA includes the catalytic domain, linker region and starch binding domain having the amino acid sequence of SEQ ID NO: 2. As used herein, the terms “glucoamylase variant” and “variant” are used in reference to glucoamylases that have some degree of amino acid sequence identity to a parent glucoamylase sequence. A variant is similar to a parent sequence, but has at least one substitution, deletion or insertion in their amino acid sequence that makes them different in sequence from a parent glucoamylase. In some cases, variants have been manipulated and/or engineered to include at least one substitution, deletion, or insertion in their amino acid sequence that makes them different in sequence from a parent. Additionally, a glucoamylase variant may retain the functional characteristics of the parent glucoamylase, e.g., maintaining a glucoamylase activity that is at least about 50%, about 60%, about 70%, about 80%, or about 90% of that of the parent glucoamylase. Can also have higher activity than 100% if that is what one has selected for. “Variants” may have at least about 45%, about 50%, about 55%, about 60%, about 65%, about 70%, about 75%, about 80%, about 85%, about 88%, about 90%, about 91%, about 92%, about 93%, about 94%, about 95%, about 96%, about 97%, about 98%, about 99%, or about 99.5% sequence identity to a parent polypeptide sequence when optimally aligned for comparison. In some embodiments, the glucoamylase variant may have at least about 45%, about 50%, about 55%, about 60%, about 65%, about 70%, about 75%, about 80%, about 85%, about 88%, about 90%, about 91%, about 92%, about 93%, about 94%, about 95%, about 96%, about 97%, about 98%, about 99%, or about 99.5% sequence identity to the catalytic domain of a parent glucoamylase. In some embodiments, the glucoamylase variant may have at least at least about 45%, about 50%, about 55%, about 60%, about 65%, about 70%, about 75%, about 80%, about 85%, about 88%, about 90%, about 91%, about 92%, about 93%, about 94%, about 95%, about 96%, about 97%, about 98%, about 99%, or about 99.5% sequence identity to the starch binding domain of a parent glucoamylase. The sequence identity can be measured over the entire length of the parent or the variant sequence. Sequence identity is determined using standard techniques known in the art (see e.g., Smith and Waterman, The “percent (%) nucleic acid sequence identity” or “percent (%) amino acid sequence identity” is defined as the percentage of nucleotide residues or amino acid residues in a candidate sequence that are identical with the nucleotide residues or amino acid residues of the starting sequence (e.g., SEQ ID NO 2). The sequence identity can be measured over the entire length of the starting sequence. “Sequence identity” is determined herein by the method of sequence alignment. For the purpose of the present disclosure, the alignment method is BLAST described by Altschul et al., (Altschul et al., The term “optimal alignment” refers to the alignment giving the highest percent identity score. As used herein the term “catalytic domain” refers to a structural region of a polypeptide, which contains the active site for substrate hydrolysis. The term “linker” refers to a short amino acid sequence generally having between 3 and 40 amino acids residues that covalently bind an amino acid sequence comprising a starch binding domain with an amino acid sequence comprising a catalytic domain. The term “starch binding domain” refers to an amino acid sequence that binds preferentially to a starch substrate. As used herein, the terms “mutant sequence” and “mutant gene” are used interchangeably and refer to a polynucleotide sequence that has an alteration in at least one codon occurring in a host cell's parent sequence. The expression product of the mutant sequence is a variant protein with an altered amino acid sequence relative to the parent. The expression product may have an altered functional capacity (e.g., enhanced enzymatic activity). The term “property” or grammatical equivalents thereof in the context of a polypeptide, as used herein, refers to any characteristic or attribute of a polypeptide that can be selected or detected. These properties include, but are not limited to oxidative stability, substrate specificity, catalytic activity, thermal stability, pH activity profile, resistance to proteolytic degradation, KM, KCAT, KCAT/KM ratio, protein folding, ability to bind a substrate and ability to be secreted. The term “property” or grammatical equivalent thereof in the context of a nucleic acid, as used herein, refers to any characteristic or attribute of a nucleic acid that can be selected or detected. These properties include, but are not limited to, a property affecting gene transcription (e.g., promoter strength or promoter recognition), a property affecting RNA processing (e.g., RNA splicing and RNA stability), a property affecting translation (e.g., regulation, binding of mRNA to ribosomal proteins). The terms “thermally stable” and “thermostable” refer to glucoamylase variants of the present disclosure that retain a specified amount of enzymatic activity after exposure to a temperature over a given period of time under conditions prevailing during the hydrolysis of starch substrates, for example, while exposed to altered temperatures. The term “enhanced stability” in the context of a property such as thermostability refers to a higher retained starch hydrolytic activity over time as compared to another reference (i.e., parent) glucoamylase. The term “diminished stability” in the context of a property such as thermostability refers to a lower retained starch hydrolytic activity over time as compared to another reference glucoamylase. The term “specific activity” is defined as the activity per mg of glucoamylase protein. In some embodiments, the activity for glucoamylase is determined by the ethanol assay described herein and expressed as the amount of glucose that is produced from the starch substrate. In some embodiments, the protein concentration can be determined using the Caliper assay described herein. The terms “active” and “biologically active” refer to a biological activity associated with a particular protein. It follows that the biological activity of a given protein refers to any biological activity typically attributed to that protein by those skilled in the art. For example, an enzymatic activity associated with a glucoamylase is hydrolytic and, thus an active glucoamylase has hydrolytic activity. The terms “polynucleotide” and “nucleic acid”, used interchangeably herein, refer to a polymeric form of nucleotides of any length, either ribonucleotides or deoxyribonucleotides. These terms include, but are not limited to, a single-, double- or triple-stranded DNA, genomic DNA, cDNA, RNA, DNA-RNA hybrid, or a polymer comprising purine and pyrimidine bases, or other natural, chemically, biochemically modified, non-natural or derivatized nucleotide bases. As used herein, the terms “DNA construct,” “transforming DNA” and “expression vector” are used interchangeably to refer to DNA used to introduce sequences into a host cell or organism. The DNA may be generated in vitro by PCR or any other suitable technique(s) known to those in the art. The DNA construct, transforming DNA or recombinant expression cassette can be incorporated into a plasmid, chromosome, mitochondrial DNA, plastid DNA, virus, or nucleic acid fragment. Typically, the recombinant expression cassette portion of an expression vector, DNA construct or transforming DNA includes, among other sequences, a nucleic acid sequence to be transcribed and a promoter. In some embodiments, expression vectors have the ability to incorporate and express heterologous DNA fragments in a host cell. As used herein, the term “vector” refers to a polynucleotide construct designed to introduce nucleic acids into one or more cell types. Vectors include cloning vectors, expression vectors, shuttle vectors, plasmids, cassettes, and the like. As used herein in the context of introducing a nucleic acid sequence into a cell, the term “introduced” refers to any method suitable for transferring the nucleic acid sequence into the cell. Such methods for introduction include but are not limited to protoplast fusion, transfection, transformation, conjugation, and transduction. As used herein, the terms “transformed” and “stably transformed” refers to a cell that has a non-native (heterologous) polynucleotide sequence integrated into its genome or as an episomal plasmid that is maintained for at least two generations. As used herein, the terms “selectable marker” and “selective marker” refer to a nucleic acid (e.g., a gene) capable of expression in host cells that allows for ease of selection of those hosts containing the vector. Typically, selectable markers are genes that confer antimicrobial resistance or a metabolic advantage on the host cell to allow cells containing the exogenous DNA to be distinguished from cells that have not received any exogenous sequence during the transformation. As used herein, the term “promoter” refers to a nucleic acid sequence that functions to direct transcription of a downstream gene. The promoter, together with other transcriptional and translational regulatory nucleic acid sequences (also termed “control sequences”) is necessary to express a given gene. In general, the transcriptional and translational regulatory sequences include, but are not limited to, promoter sequences, ribosomal binding sites, transcriptional start and stop sequences, translational start and stop sequences, and enhancer or activator sequences. A nucleic acid is “operably linked” when it is placed into a functional relationship with another nucleic acid sequence. For example, DNA encoding a secretory leader (i.e., a signal peptide), is operably linked to DNA for a polypeptide if it is expressed as a preprotein that participates in the secretion of the polypeptide. Generally, “operably linked” means that the DNA sequences being linked are contiguous, and, in the case of a secretory leader, contiguous and in reading phase. As used herein the term “gene” refers to a polynucleotide (e.g., a DNA segment), that encodes a polypeptide and includes regions preceding and following the coding regions, as well as intervening sequences (introns) between individual coding segments (exons). As used herein, “ortholog” and “orthologous genes” refer to genes in different species that have evolved from a common ancestral gene (i.e., a homologous gene) by speciation. Typically, orthologs retain the same function during the course of evolution. Identification of orthologs finds use in the reliable prediction of gene function in newly sequenced genomes. As used herein, “paralog” and “paralogous genes” refer to genes that are related by duplication within a genome. While orthologs retain the same function through the course of evolution, paralogs evolve new functions, even though some functions are often related to the original one. Examples of paralogous genes include, but are not limited to genes encoding trypsin, chymotrypsin, elastase, and thrombin, which are all serine proteinases and occur together within the same species. As used herein, the term “hybridization” refers to the process by which a strand of nucleic acid joins with a complementary strand through base pairing, as known in the art. A nucleic acid sequence is considered to be “selectively hybridizable” to a reference nucleic acid sequence if the two sequences specifically hybridize to one another under moderate to high stringency hybridization and wash conditions. Hybridization conditions are based on the melting temperature (Tm) of the nucleic acid binding complex or probe. For example, “maximum stringency” typically occurs at about Tm−5° C. (5° C. below the Tm of the probe); “high stringency” at about 5-10° C. below the Tm; “intermediate stringency” at about 10-20° C. below the Tm of the probe; and “low stringency” at about 20-25° C. below the Tm. Functionally, maximum stringency conditions may be used to identify sequences having strict identity or near-strict identity with the hybridization probe; while an intermediate or low stringency hybridization can be used to identify or detect polynucleotide sequence homologs. Moderate and high stringency hybridization conditions are well known in the art. An example of high stringency conditions includes hybridization at about 42° C. in 50% formamide, 5×SSC, 5×Denhardt's solution, 0.5% SDS and 100 μg/ml denatured carrier DNA followed by washing two times in 2×SSC and 0.5% SDS at room temperature and two additional times in 0.1×SSC and 0.5% SDS at 42° C. An example of moderate stringent conditions include an overnight incubation at 37° C. in a solution comprising 20% formamide, 5×SSC (150 mM NaCl, 15 mM trisodium citrate), 50 mM sodium phosphate (pH 7.6), 5×Denhardt's solution, 10% dextran sulfate and 20 mg/ml denaturated sheared salmon sperm DNA, followed by washing the filters in 1×SSC at about 37-50° C. Those of skill in the art know how to adjust the temperature, ionic strength, etc. as necessary to accommodate factors such as probe length and the like. As used herein, “recombinant” includes reference to a cell or vector, that has been modified by the introduction of a heterologous or homologous nucleic acid sequence or that the cell is derived from a cell so modified. Thus, for example, recombinant cells express genes that are not found in identical form within the native (non-recombinant) form of the cell or express native genes that are otherwise abnormally expressed, under expressed or not expressed at all as a result of deliberate human intervention. In an embodiment of the disclosure, mutated DNA sequences are generated with site saturation mutagenesis in at least one codon. In another embodiment, site saturation mutagenesis is performed for two or more codons. In a further embodiment, mutant DNA sequences have more than about 50%, about 55%, about 60%, about 65%, about 70%, about 75%, about 80%, about 85%, about 90%, about 95%, or about 98% identity with the parent sequence. In alternative embodiments, mutant DNA is generated in vivo using any known mutagenic procedure such as, for example, radiation, nitrosoguanidine, and the like. The desired DNA sequence is then isolated and used in the methods provided herein. As used herein, “heterologous protein” refers to a protein or polypeptide that does not naturally occur in the host cell. An enzyme is “over-expressed” in a host cell if the enzyme is expressed in the cell at a higher level than the level at which it is expressed in a corresponding wild-type cell. The terms “protein” and “polypeptide” are used interchangeability herein. In the present disclosure and claims, the conventional one-letter and three-letter codes for amino acid residues are used. The 3-letter code for amino acids as defined in conformity with the IUPAC-IUB Joint Commission on Biochemical Nomenclature (JCBN). It is also understood that a polypeptide may be coded for by more than one nucleotide sequence due to the degeneracy of the genetic code. Variants of the disclosure are described by the following nomenclature: [original amino acid residue/position/substituted amino acid residue]. For example, the substitution of leucine for arginine at position 76 is represented as R76L. When more than one amino acid is substituted at a given position, the substitution is represented as 1) Q172C, Q172D or Q172R; 2) Q172C, D, or R, or 3) Q172C/D/R. When a position suitable for substitution is identified herein without a specific amino acid suggested, it is to be understood that any amino acid residue may be substituted for the amino acid residue present in the position. Where a variant glucoamylase contains a deletion in comparison with other glucoamylases the deletion is indicated with “*”. For example, a deletion at position R76 is represented as R76*. A deletion of two or more consecutive amino acids is indicated for example as (76-78)*. A “prosequence” is an amino acid sequence between the signal sequence and mature protein that is necessary for the secretion of the protein. Cleavage of the pro sequence will result in a mature active protein. The term “signal sequence” or “signal peptide” refers to any sequence of nucleotides and/or amino acids that may participate in the secretion of the mature or precursor forms of the protein. This definition of signal sequence is a functional one, meant to include all those amino acid sequences encoded by the N-terminal portion of the protein gene, which participate in the effectuation of the secretion of protein. They are often, but not universally, bound to the N-terminal portion of a protein or to the N-terminal portion of a precursor protein. The signal sequence may be endogenous or exogenous. The signal sequence may be that normally associated with the protein (e.g., glucoamylase), or may be from a gene encoding another secreted protein. The term “precursor” form of a protein or peptide refers to a mature form of the protein having a prosequence operably linked to the amino or carbonyl terminus of the protein. The precursor may also have a “signal” sequence operably linked, to the amino terminus of the prosequence. The precursor may also have additional polynucleotides that are involved in post-translational activity (e.g., polynucleotides cleaved therefrom to leave the mature form of a protein or peptide). “Host strain” or “host cell” refers to a suitable host for an expression vector comprising DNA according to the present disclosure. The terms “derived from” and “obtained from” refer to not only a glucoamylase produced or producible by a strain of the organism in question, but also a glucoamylase encoded by a DNA sequence isolated from such strain and produced in a host organism containing such DNA sequence. Additionally, the term refers to a glucoamylase that is encoded by a DNA sequence of synthetic and/or cDNA origin and that has the identifying characteristics of the glucoamylase in question. A “derivative” within the scope of this definition generally retains the characteristic hydrolyzing activity observed in the wild-type, native or parent form to the extent that the derivative is useful for similar purposes as the wild-type, native or parent form. Functional derivatives of glucoamylases encompass naturally occurring, synthetically or recombinantly produced peptides or peptide fragments that have the general characteristics of the glucoamylases of the present disclosure. The term “isolated” refers to a material that is removed from the natural environment if it is naturally occurring. A “purified” protein refers to a protein that is at least partially purified to homogeneity. In some embodiments, a purified protein is more than about 10% pure, about 20% pure, or about 30% pure, as determined by SDS-PAGE. Further aspects of the disclosure encompass the protein in a highly purified form (i.e., more than about 40% pure, about 60% pure, about 80% pure, about 90% pure, about 95% pure, about 97% pure, or about 99% pure), as determined by SDS-PAGE. As used herein, the term, “combinatorial mutagenesis” refers to methods in which libraries of variants of a starting sequence are generated. In these libraries, the variants contain one or several mutations chosen from a predefined set of mutations. In addition, the methods provide means to introduce random mutations that were not members of the predefined set of mutations. In some embodiments, the methods include those set forth in U.S. Pat. No. 6,582,914, hereby incorporated by reference. In alternative embodiments, combinatorial mutagenesis methods encompass commercially available kits (e.g., QuikChange® Multisite, Stratagene, San Diego, Calif.). As used herein, the term “library of mutants” refers to a population of cells that are identical in most of their genome but include different homologues of one or more genes. Such libraries can be used, for example, to identify genes or operons with improved traits. As used herein the term “dry solids content (DS or ds)” refers to the total solids of a slurry in % on a dry weight basis. As used herein, the term “initial hit” refers to a variant that was identified by screening a combinatorial consensus mutagenesis library. In some embodiments, initial hits have improved performance characteristics, as compared to the starting gene. As used herein, the term “improved hit” refers to a variant that was identified by screening an enhanced combinatorial consensus mutagenesis library. As used herein, the term “target property” refers to the property of the starting gene that is to be altered. It is not intended that the present disclosure be limited to any particular target property. However, in some embodiments, the target property is the stability of a gene product (e.g., resistance to denaturation, proteolysis or other degradative factors), while in other embodiments, the level of production in a production host is altered. Indeed, it is contemplated that any property of a starting gene will find use in the present disclosure. Other definitions of terms may appear throughout the specification. As used herein, the “process for making beer” may further be applied in the mashing of any grist. As used herein, the term “grist” refers to any starch and/or sugar containing plant material derivable from any plant and plant part, including tubers (e.g. potatoes), roots (e.g. cassaya [ The term “adjunct” is understood as the part of the grist which is not barley malt. The adjunct may be any carbohydrate rich material. In term “adjunct” includes starch and/or sugar containing plant material as e.g. defined above under “grist”. The term “fermentation” means, in the context of brewing, the transformation of sugars in the wort, by enzymes in the brewing yeast, into ethanol and carbon dioxide with the formation of other fermentation by-products. As used herein the term “malt” is understood as any malted cereal grain, such as barley. As used herein, the term “malt beverage” includes such foam forming fermented malt beverages as full malted beer, ale, dry beer, near beer, light beer, low alcohol beer, low calorie beer, porter, bock beer, stout, malt liquor, non-alcoholic malt liquor and the like. The term “malt beverages” also includes non-foaming beer and alternative malt beverages such as fruit flavoured malt beverages, e.g., citrus flavoured, such as lemon-, orange-, lime-, or berry-flavoured malt beverages, liquor flavoured malt beverages, e.g., vodka-, rum-, or tequila-flavoured malt liquor, or coffee flavoured malt beverages, such as caffeine-flavoured malt liquor, and the like. The term “mash” is understood as aqueous starch slurry, e.g. comprising crushed barley malt, crushed barley, and/or other adjunct or a combination hereof, mixed with water later to be separated into wort+spent grains. As used herein, the term “wort” refers to the unfermented liquor run-off following extracting the grist during mashing. As used herein, the term “spent grains” refers to the drained solids remaining when the grist has been extracted and the wort separated from the mash. Included within the term “beer” is any fermented wort, produced by the brewing and fermentation of a starch-containing material, mainly derived from cereal grains, such as malted barley. Wheat, maize, and rice may also be used. As used herein, the term “extract recovery” in the wort is defined as the sum of soluble substances extracted from the grist (malt and adjuncts) expressed in percentage based on dry matter. As used herein, the term “pasteurization” means heating (e.g. beer) at certain temperatures for certain time intervals. The purpose is normally killing of micro-organisms but pasteurization can also cause inactivation of enzyme activity. Implementation of pasteurisation in the brewing process is typically through the use of a flash pasteuriser or tunnel pasteuriser. As used herein, the term “pasteurisation units or PU” refers to a quantitative measure of pasteurisation. One pasteurisation unit (1 PU) for beer is defined as a heat retention of one minute at 60 degrees Celsius. One calculates that: Different minimum PU may be used depending on beer type, raw materials and microbial contamination, brewer and perceived effect on beer flavour. Typically, for beer pasteurisation, 14-15 PU are required. Depending on the pasteurising equipment, pasteurisation temperatures are typically in the range of 64-72 degrees Celsius with a pasteurisation time calculated accordingly. Further information may be found in “Technology Brewing and Malting” by Wolfgang Kunze of the Research and Teaching Institute of Brewing, Berlin (VLB), 3rd completely updated edition, 2004, ISBN 3-921690-49-8. As used herein, the term “non-alcoholic beer” or “low-alcohol beer” refers to a beer containing a maximum of 0.1% to 3.5% or 0.1% to 2.5% such as 0.1% to 0.5% alcohol by volume. Non-alcoholic beer is brewed by traditional methods, but during the finishing stages of the brewing process the alcohol is removed by vacuum evaporation, by taking advantage of the different boiling points of water and alcohol. As used herein, the term “low-calorie beer” or “beer with a low carbohydrate content” is defined as a beer with a carbohydrate content of 1.5 g/100 g or less and with a real degree of fermentation of at least 80%. Where a range of values is provided, it is understood that each intervening value, to the tenth of the unit of the lower limit unless the context clearly dictates otherwise, between the upper and lower limits of that range is also specifically disclosed. Each smaller range between any stated value or intervening value in a stated range and any other stated or intervening value in that stated range is encompassed within the disclosure. The upper and lower limits of these smaller ranges may independently be included or excluded in the range, and each range where either, neither or both limits are included in the smaller ranges is also encompassed within the disclosure, subject to any specifically excluded limit in the stated range. Where the stated range includes one or both of the limits, ranges excluding either or both of those included limits are also included in the disclosure. Before the exemplary embodiments are described in more detail, it is to be understood that this disclosure is not limited to particular embodiments described, as such may, of course, vary. Although any methods and materials similar or equivalent to those described herein can be used in the practice or testing of the present disclosure, exemplary methods and materials are now described. As used herein and in the appended claims, the singular forms “a”, “an”, and “the” include plural referents unless the context clearly dictates otherwise. Thus, for example, reference to “a gene” includes a plurality of such candidate agents and reference to “the cell” includes reference to one or more cells and equivalents thereof known to those skilled in the art, and so forth. The publications discussed herein are provided solely for their disclosure prior to the filing date of the present application. Nothing herein is to be construed as an admission that the present disclosure is not entitled to antedate such publication by virtue of prior invention. GA glucoamylase
EtOH ethanol
DP1 monosaccharides
In some embodiments, the present disclosure provides a glucoamylase variant. The glucoamylase variant is a variant of a parent glucoamylase, which may comprise both a catalytic domain and a starch binding domain. In some embodiments, the parent glucoamylase comprises a catalytic domain having an amino acid sequence as illustrated in SEQ ID NO: 1, 2, 3, 5, 6, 7, 8 or 9 or having an amino acid sequence displaying at least about 80%, about 85%, about 90%, about 95%, about 97%, about 99%, or about 99.5% sequence identity with one or more of the amino acid sequences illustrated in SEQ ID NO: 1, 2, 3, 5, 6, 7, 8, or 9. In yet other embodiments, the parent glucoamylase comprises a catalytic domain encoded by a DNA sequence that hybridizes under medium, high, or stringent conditions with a DNA encoding the catalytic domain of a glucoamylase having one of the amino acid sequences of SEQ ID NO: 1, 2 or 3. In some embodiments, the parent glucoamylase comprises a starch binding domain having an amino acid sequence as illustrated in SEQ ID NO 1, 2, 11, 385, 386, 387, 388, 389, or 390, or having an amino acid sequence displaying at least about 80%, about 85%, about 90%, about 95%, about 97%, about 99%, or about 99.5% sequence identity with one or more of the amino acid sequence illustrated in SEQ ID NO 1, 2, 11, 385, 386, 387, 388, 389, or 390. In yet other embodiments, the parent glucoamylase comprises a starch binding domain encoded by a DNA sequence that hybridizes under medium, high, or stringent conditions with a DNA encoding the starch binding domain of a glucoamylase having one of the amino acid sequences of SEQ ID NO: 1, 2, or 11. Predicted structure and known sequences of glucoamylases are conserved among fungal species (Coutinho et al., 1994 In some embodiments, the parent glucoamylase may be a bacterial glucoamylase. For example, the polypeptide may be obtained from a gram-positive bacterial strain such as In some embodiments, the parent glucoamylase will comprise a catalytic domain having at least about 80%, about 85%, about 90%, about 93%, about 95%, about 97%, about 98%, or about 99% sequence identity with the catalytic domain of the TrGA amino acid sequence of SEQ ID NO: 3. In other embodiments, the parent glucoamylase will comprise a catalytic domain having at least about 90%, about 93%, about 95%, about 96%, about 97%, about 98%, or about 99% sequence identity with the catalytic domain of the In yet other embodiments, the parent glucoamylase will comprise a catalytic domain having at least about 90%, about 95%, about 97%, or about 99% sequence identity with the catalytic domain of the In some embodiments, the parent glucoamylase will comprise a starch binding domain having at least about 80%, about 85%, about 90%, about 95%, about 97%, or about 98% sequence identity with the starch binding domain of the TrGA amino acid sequence of SEQ ID NO: 1, 2, or 11. In other embodiments, the parent glucoamylase will comprise a starch binding domain having at least about 90%, about 95%, about 97%, or about 99% sequence identity with the catalytic domain of the In other embodiments, the parent glucoamylase will comprise a starch binding domain having at least about 90%, about 95%, about 97%, or about 99% sequence identity with the catalytic domain of the In other embodiments, the parent glucoamylase will comprise a starch binding domain having at least about 90%, about 95%, about 97%, or about 99% sequence identity with the catalytic domain of the In other embodiments, the parent glucoamylase will comprise a starch binding domain having at least about 90%, about 95%, about 97%, or about 99% sequence identity with the catalytic domain of the In yet other embodiments, the parent glucoamylase will comprise a starch binding domain having at least about 90%, about 93%, about 95%, about 96%, about 97%, about 98%, or about 99% sequence identity with the starch binding domain of the In some embodiments, the parent glucoamylase will have at least about 80%, about 85%, about 88%, about 90%, about 93%, about 95%, about 96%, about 97%, about 98%, or about 99% sequence identity with the TrGA amino acid sequence of SEQ ID NO: 1 or 2. In further embodiments, a In some embodiments, the parent glucoamylase is TrGA comprising the amino acid sequence of SEQ ID NO: 2, or a A parent glucoamylase can be isolated and/or identified using standard recombinant DNA techniques. Any standard techniques can be used that are known to the skilled artisan. For example, probes and/or primers specific for conserved regions of the glucoamylase can be used to identify homologs in bacterial or fungal cells (the catalytic domain, the active site, etc.). Alternatively, degenerate PCR can be used to identify homologues in bacterial or fungal cells. In some cases, known sequences, such as in a database, can be analyzed for sequence and/or structural identity to one of the known glucoamylases, including SEQ ID NO: 2, or a known starch binding domains, including SEQ ID NO: 11. Functional assays can also be used to identify glucoamylase activity in a bacterial or fungal cell. Proteins having glucoamylase activity can be isolated and reverse sequenced to isolate the corresponding DNA sequence. Such methods are known to the skilled artisan. The central dogma of molecular biology is that the sequence of DNA encoding a gene for a particular enzyme, determines the amino acid sequence of the protein, this sequence in turn determines the three-dimensional folding of the enzyme. This folding brings together disparate residues that create a catalytic center and substrate binding surface and this results in the high specificity and activity of the enzymes in question. Glucoamylases consist of as many as three distinct structural domains, a catalytic domain of approximately 450 residues that is structurally conserved in all glucoamylases, generally followed by a linker region consisting of between 30 and 80 residues that are connected to a starch binding domain of approximately 100 residues. The structure of the The catalytic domain of TrGA thus has approximately 450 residues such as residues 1-453 of TrGA SEQ ID NO:2 and is a twelve helix double barrel domain. The helices and loops of the catalytic domain can be defined in terms of the residues of TrGA with SEQ ID NO:2 forming them: The linker domain has between 30 and 80 residues such as residues 454-490 of TrGA with SEQ ID NO: 2. The starch binding domain of TrGA has approximately 100 residues such as residues 496-596 of TrGA with SEQ ID NO:2 consisting of the beta sandwich composed of two twisted three stranded sheets. The sheets, helices and loops of the starch binding domain can be defined in terms of the residues of TrGA with SEQ ID NO:2 forming them: It is possible to identify equivalent residues based on structural superposition in other glucoamylases as described in further detail below. A further crystal structure was produced using the coordinates in Table 20 in WO2009/067218 (Danisco US Inc., Genencor Division) page 94-216 incorporated herein by reference for the Starch Binding Domain (SBD). The SBD for TrGA was aligned with the SBD for Thus, the amino acid position numbers discussed herein refer to those assigned to the mature “Structural identity” determines whether the amino acid residues are equivalent. Structural identity is a one-to-one topological equivalent when the two structures (three dimensional and amino acid structures) are aligned. A residue (amino acid) position of a glucoamylase is “equivalent” to a residue of In order to establish identity to the primary structure, the amino acid sequence of a glucoamylase can be directly compared to For example, in Structural identity involves the identification of equivalent residues between the two structures. “Equivalent residues” can be defined by determining homology at the level of tertiary structure (structural identity) for an enzyme whose tertiary structure has been determined by X-ray crystallography. Equivalent residues are defined as those for which the atomic coordinates of two or more of the main chain atoms of a particular amino acid residue of the Equivalent residues that are functionally analogous to a specific residue of Some of the residues identified for substitution are conserved residues whereas others are not. In the case of residues that are not conserved, the substitution of one or more amino acids is limited to substitutions that produce a variant that has an amino acid sequence that does not correspond to one found in nature. In the case of conserved residues, such substitutions should not result in a naturally-occurring sequence. The variants according to the disclosure include at least one substitution, deletion or insertion in the amino acid sequence of a parent glucoamylase that makes the variant different in sequence from a parent glucoamylase. In some embodiments, the variants of the disclosure will have at least about 20%, about 40%, about 50%, about 60%, about 70%, about 80%, about 8S %, about 90%, about 95%, about 97%, or about 100% of the glucoamylase activity as that of the TrGA (SEQ ID NO: 2), a parent glucoamylase that has at least 80% sequence identity to TrGA (SEQ ID NO: 2). In some embodiments, the variants according to the disclosure will comprise a substitution, deletion or insertion in at least one amino acid position of the parent TrGA (SEQ ID NO: 2), or in an equivalent position in the sequence of another parent glucoamylase having at least about 80%, about 85%, about 90%, about 95%, about 97%, about 98%, or about 99% sequence identity to the TrGA sequence (SEQ ID NO: 2). In other embodiments, the variant according to the disclosure will comprise a substitution, deletion or insertion in at least one amino acid position of a fragment of the parent TrGA, wherein the fragment comprises the catalytic domain of the TrGA sequence (SEQ ID NO: 3) or in an equivalent position in a fragment comprising the catalytic domain of a parent glucoamylase having at least about 80%, about 85%, about 90%, about 95%, about 97%, about 98%, or about 99% sequence identity to the catalytic-domain-containing fragment of the SEQ ID NO: 3, 5, 6, 7, 8, or 9. In some embodiments, the fragment will comprise at least about 400, about 425, about 450, or about 500 amino acid residues of TrGA catalytic domain (SEQ ID NO: 3). In other embodiments, the variant according to the disclosure will comprise a substitution, deletion or insertion in at least one amino acid position of a fragment of the parent TrGA, wherein the fragment comprises the starch binding domain of the TrGA sequence (SEQ ID NO: 11) or in an equivalent position in a fragment comprising the starch binding domain of a parent glucoamylase having at least about 80%, about 85%, about 90%, about 95%, about 97%, about 98%, or about 99% sequence identity to the starch-binding-domain-containing fragment of SEQ ID NO: 11, 385, 386, 387, 388, 389, and 390. In some embodiments, the fragment will comprise at least about 40, about 50, about 60, about 70, about 80, about 90, about 100, or about 109 amino acid residues of TrGA starch binding domain (SEQ ID NO: 11). In some embodiments, when the parent glucoamylase includes a catalytic domain, a linker region, and a starch binding domain, the variant will comprise a substitution, deletion or insertion in at least one amino acid position of a fragment comprising part of the linker region. In some embodiments, the variant will comprise a substitution deletion, or insertion in the amino acid sequence of a fragment of the TrGA sequence (SEQ ID NO: 2). Structural identity with reference to an amino acid substitution means that the substitution occurs at the equivalent amino acid position in the homologous glucoamylase or parent glucoamylase. The term equivalent position means a position that is common to two parent sequences that is based on an alignment of the amino acid sequence of the parent glucoamylase in question as well as alignment of the three-dimensional structure of the parent glucoamylase in question with the TrGA reference glucoamylase amino acid sequence and three-dimensional sequence. For example, with reference to Accordingly, in one aspect, a glucoamylase variant is described, which glucoamylase variant when in its crystal form has a crystal structure for which the atomic coordinates of the main chain atoms have a root-mean-square deviation from the atomic coordinates of the equivalent main chain atoms of TrGA (as defined in Table 20 in WO2009/067218) of less than 0.13 nm following alignment of equivalent main chain atoms, and which have a linker region, a starch binding domain and a catalytic domain, said variant comprising two or more amino acid substitutions relative to the amino acid sequence of the parent glucoamylase in interconnecting loop 2′ of the starch binding domain, and/or in loop 1, and/or in helix 2, and/or in loop 11, and/or in helix 12 of the catalytic domain. In a further aspect, the root-mean-square deviation from the atomic coordinates of the equivalent main chain atoms of TrGA (as defined in Table 20 in WO2009/067218) is less than 0.12 nm, such as less than 0.11 or such as less than 0.10. In one aspect, a glucoamylase variant is described, which glucoamylase variant comprises a starch binding domain and a catalytic domain, said variant comprising two or more amino acid substitutions relative to the amino acid sequence of SEQ ID NO:2 or equivalent parent glucoamylase in interconnecting loop 2′, and/or in loop 1, and/or in helix 2, and/or in loop 11, and/or in helix 12 for reducing the synthesis of condensation products during hydrolysis of starch. In a further aspect, a glucoamylase variant is described, which glucoamylase variant comprises two or more amino acid substitutions relative to interconnecting loop 2′ with the amino acid sequence from position 518 to position 543 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or loop 1 with the amino acid sequence from position 21 to position 51 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or helix 2 with the amino acid sequence from position 52 to position 68 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or loop 11 with the amino acid sequence from position 396 to position 420 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or helix 12 with the amino acid sequence from position 421 to position 434 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase. In a further aspect, a glucoamylase variant is described, which glucoamylase variant comprises two or more amino acid substitutions relative to the amino acid sequence from position 518 to position 543 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or the amino acid sequence from position 21 to position 51 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or the amino acid sequence from position 52 to position 68 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or the amino acid sequence from position 396 to position 420 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or the amino acid sequence from position 421 to position 434 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase. In one aspect, the two or more amino acid substitutions are relative to the interconnecting loop 2′ with the amino acid sequence from position 518 to position 543 e.g. in one or more of positions 518, 519, 520, 521, 522, 523, 524, 525, 526, 527, 528, 529, 530, 531, 532, 533, 534, 535, 536, 537, 538, 539, 540, 541, 542 and/or 543 of SEQ ID NO:2, and/or loop 1 with the amino acid sequence from position 21 to position 51 e.g. in one or more of positions 21, 22, 23, 24, 25, 26, 27, 28, 29, 30, 31, 32, 33, 34, 35, 36, 37, 38, 39, 40, 41, 42, 43, 44, 45, 46, 47, 48, 49, 50 and/or 51 of SEQ ID NO:2, and/or helix 2 with the amino acid sequence from position 52 to position 68 e.g. in one or more of positions 52, 53, 54, 55, 56, 57, 58, 59, 60, 61, 62, 63, 64, 65, 66, 67 and/or 68 of SEQ ID NO:2, and/or loop 11 with the amino acid sequence from position 396 to position 420 e.g. in one or more of positions 396, 397, 398, 399, 400, 401, 402, 403, 404, 405, 406, 407, 408, 409, 410, 411, 412, 413, 414, 415, 416, 417, 418, 419 and/or 420 of SEQ ID NO:2, and/or helix 12 with the amino acid sequence from position 421 to position 434 e.g. in one or more of positions 421, 422, 423, 424, 425, 426, 427, 428, 429, 430, 431, 432, 433 and/or 534 of SEQ ID NO:2. In a further aspect, the two or more amino acid substitutions are at least one amino acid substitution in the interconnecting loop 2′ and at least one amino acid substitution in loop 1 and/or helix 2 and/or loop 11 and/or helix 12. In a further aspect, the two or more amino acid substitutions are 1, 2, 3 or 4 amino acid substitutions in the interconnecting loop 2′ and 1, 2, 3 or 4 amino acid substitutions in loop 1 and/or helix 2 and/or loop 11 and/or helix 12. In a further aspect, the two or more amino acid substitutions are at least one amino acid substitution in interconnecting loop 2′ and at least one amino acid substitution in loop 1. In a further aspect, the two or more amino acid substitutions are at least one amino acid substitution in interconnecting loop 2′ and at least one amino acid substitution in helix 2. In a further aspect, the two or more amino acid substitutions are at least one amino acid substitution in interconnecting loop 2′ and at least one amino acid substitution in loop 11. In a further aspect, the two or more amino acid substitutions are at least one amino acid substitution in interconnecting loop 2′ and at least one amino acid substitution in helix 12. In a further aspect, the two or more amino acid substitutions are at least one amino acid substitution in interconnecting loop 2′ and at least one amino acid substitution in loop 1 and at least one amino acid substitution in helix 2. In a further aspect, the glucoamylase variant has at least one amino acid substitution within position 520-543, 530-543, or 534-543 of interconnecting loop 2′, the positions corresponding to the respective position in SEQ ID NO:2 or equivalent positions in a parent glucoamylase. In a further aspect, the glucoamylase variant has at least one amino acid substitution within the amino acid sequence of position 30-50, 35-48, or 40-46 of loop 1, the positions corresponding to the respective position in SEQ ID NO:2 or equivalent positions in a parent glucoamylase. In a further aspect, the glucoamylase variant has at least one amino acid substitution within the amino acid sequence of position 50-66, 55-64, or 58-63 of helix 2, the positions corresponding to the respective position in SEQ ID NO:2 or equivalent positions in a parent glucoamylase. In a further aspect, the glucoamylase variant has at least one amino acid substitution within the amino acid sequence of position 405-420, 410-420, or 415-420 of loop 11, the positions corresponding to the respective position in SEQ ID NO:2 or equivalent positions in a parent glucoamylase. In a further aspect, the glucoamylase variant has at least one amino acid substitution within the amino acid sequence of position 421-434, 425-434, or 428-434 of helix 12, the positions corresponding to the respective position in SEQ ID NO:2 or equivalent positions in a parent glucoamylase. In one aspect, the glucoamylase variant comprises two or more amino acid substitutions, wherein an amino acid substitution is in position 539 and an amino acid substitution is in position 44, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase, and which sequence has at least 80% sequence identity to the parent glucoamylase, and wherein the amino acid substitution in position 44 is not 44C. In a further aspect, the glucoamylase variant comprises two or more amino acid substitutions, wherein an amino acid substitution is in position 539 and an amino acid substitution is 44R, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In a further aspect, the glucoamylase variant comprises an amino acid substitution in position 61, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In a further aspect, the amino acid substitution in position 539 is 539R, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In a further aspect, the amino acid substitution in position 44 is 44R, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In a further aspect, the amino acid substitution in position 61 is 61I, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In a further aspect, the glucoamylase variant comprises the following amino acid substitutions: the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. In a further aspect, the glucoamylase variant consist of SEQ ID NO:2 and has the following amino acid substitutions: the positions corresponding to the respective position in SEQ ID NO:2. In a further aspect, the glucoamylase variant has a starch binding domain that has at least 96%, 97%, 98%, 99%, or 99.5% sequence identity with the starch binding domain of SEQ ID NO: 1, 2, 11, 385, 386, 387, 388, 389, or 390. In a further aspect, the glucoamylase variant has a catalytic domain that has at least 80%, 85%, 90%, 95%, or 99.5% sequence identity with the catalytic domain of SEQ ID NO: 1, 2, 3, 5, 6, 7, 8, or 9. In a further aspect, the parent glucoamylase is a fungal glucoamylase. In a further aspect, the parent glucoamylase is selected from a glucoamylase obtained from a In a further aspect, the parent glucoamylase is obtained from a In a further aspect, the glucoamylase has been purified. The glucoamylases of the present disclosure may be recovered or purified from culture media by a variety of procedures known in the art including centrifugation, filtration, extraction, precipitation and the like. In some embodiments, the glucoamylase variant will include at least two substitutions in the amino acid sequence of a parent. In further embodiments, the variant may have more than two substitutions. For example, the variant may have 2, 3, 4, 5, 6, 7, 8, 9, 10, 15, 20, or 25 amino acid substitutions, deletions, or insertions as compared to a corresponding parent glucoamylase. In some embodiments, a glucoamylase variant comprises a substitution, deletion or insertion, and typically a substitution in at least one amino acid position in a position corresponding to the regions of non-conserved amino acids as illustrated in While the variants may have substitutions in any position of the mature protein sequence (SEQ ID NO: 2), in some embodiments, a glucoamylase variant comprises two or more substitutions in the following positions in the amino acid sequence set forth in SEQ ID NO: 2: 23, 42, 43, 44, 59, 60, 61, 65, 67, 68, 410, 417, 418, 430, 431, 433, 518, 519, 520, 527, 531, 535, 536, 537 or 539, or in an equivalent position in a parent glucoamylase. In a further aspect, the glucoamylase variant comprises one or more further substitutions in the following positions in the amino acid sequence set forth in SEQ ID NO: 2: 10, 14, 15, 72, 73, 97, 98, 99, 102, 110, 113, 114, 133, 140, 144, 145, 147, 152, 153, 164, 182, 204, 205, 214, 216, 219, 228, 229, 230, 231, 236, 239, 241, 242, 263, 264, 265, 268, 269, 276, 284, 291, 294, 300, 301, 303, 311, 338, 342, 344, 346, 349, 359, 361, 364, 375, 379, 382, 390, 391, 393, 394, 436, 442, 444, 448, 451, 493, 494, 495, 502, 503, 508, 511, 563, or 577, or in an equivalent position in a parent glucoamylase. In some embodiments, the parent glucoamylase will have at least about 50%, about 60%, about 70%, about 80%, about 90%, about 95%, about 96%, about 97%, about 98%, or about 99% sequence identity with SEQ ID NO: 2. In other embodiments, the parent glucoamylase will be a In some embodiments, the glucoamylase variant comprises two or more substitutions in the following positions in the amino acid sequence set forth in SEQ ID NO: 2: P23, T42, I43, D44, P45, D46, F59, K60, N61, T67, E68, R408, S410, S415, L417, H418, T430, A431, R433, N518, A519, A520, T527, V531, A535, V536, N537, and A539 or an equivalent position in parent glucoamylase (e.g., a In some embodiments, the glucoamylase variant may differ from the parent glucoamylase only at the specified positions. In further embodiments, the variant of a glucoamylase parent comprises at least two of the following substitutions in the following positions in an amino acid sequence set forth in SEQ ID NO: 2: T42V, I43Q/R, D44R/C, N61I, T67M, E68C/M, L417K/R/V, T430A/K, A431I/L/Q, R433C/E/G/L/N/S/V/Y, A519I/K/R/Y, A520C/L/P, V531L, A535K/N/P/R, V536M, or A539E/R/S, or a substitution in an equivalent position in a parent glucoamylase. In a further aspect, the glucoamylase variant comprises one or more substitutions in the following positions in the amino acid sequence set forth in SEQ ID NO: 2: T10S, A72Y, G73F/W, S97N, S102A/M/R, K114M/Q, I133T/V, N1451, N153A/D/E/M/S/V, T205Q, Q2195, W228A/F/H/M/V, V229I/L, S230C/F/G/L/N/Q/R, S231L/V, D236R, I239V/Y, N263P, L264D/K, A268C/D/G/K, S291A/F/H/M/T, g294c, A301P/R, V3381/N/Q, T342V, S344M/P/Q/R/V, G361D/E/F/I/L/M/P/S/W/Y, A364D/E/F/G/K/L/M/R/S/T/V/W, T375N, K394S, 1436H, T451K, T495K/M/S, E503A/C/V, Q508R, Q511H, N563C/E/I/K/K/Q/T/V, or N577K/P/R, or in an equivalent position in a parent glucoamylase. In further embodiments, the glucoamylase variant comprises one of the following sets of substitutions, at the relevant positions of SEQ ID NO: 2, or at equivalent positions in a parent glucoamylase: I43R/N61I/L417V/A431L/A539R; In further embodiments, the glucoamylase variant comprises one of the following sets of substitutions, at positions of SEQ ID NO: 2 or equivalent positions in a parent glucoamylase: wherein the glucoamylase variant does not have any further substitutions relative to the parent glucoamylase, and wherein the parent glucoamylase has a catalytic domain that has at least 80% sequence identity with SEQ ID NO: 1, 2, 3, 5, 6, 7, 8, or 9. Thus the parent glucoamylase may be any of those described elsewhere. The parent glucoamylase may comprise a starch binding domain that has at least 95% sequence identity with SEQ ID NO: 1, 2, 11, 385, 386, 387, 388, 389, or 390. The parent glucoamylase may have at least 80% sequence identity with SEQ ID NO: 1 or 2; for example it may comprise SEQ ID NO: 1 or 2. Optionally the parent glucoamylase may consist of SEQ ID NO: 1 or 2. Glucoamylase variants of the disclosure may also include chimeric or hybrid glucoamylases with, for example a starch binding domain (SBD) from one glucoamylase and a catalytic domain and linker from another. For example, a hybrid glucoamylase can be made by swapping the SBD from AnGA (SEQ ID NO: 6) with the SBD from TrGA (SEQ ID NO: 2), making a hybrid with the AnGA SBD and the TrGA catalytic domain and linker. Alternatively, the SBD and linker from AnGA can be swapped for the SBD and linker of TrGA. In some aspects, the variant glucoamylase exhibits altered thermostability as compared to the parent glucoamylase. In some aspects, the altered thermostability may be increased thermostability as compared to the parent glucoamylase. In some embodiments, the altered property is altered specific activity compared to the parent glucoamylase. In some embodiments, the altered specific activity may be increased specific activity compared to the parent glucoamylase. In some embodiments, the altered property is increased thermostability at lower temperatures as compared to the parent glucoamylase. In some embodiments, the altered property is both increased specific activity and increased thermostability as compared to the parent glucoamylase. In one embodiment, some variants may include the substitutions at positions: of SEQ ID NO: 2, or equivalent positions in parent glucoamylases and particularly In a further embodiment, some variants may include the substitutions at positions: G73F/E503V/N563K/L417R/A539R; and of SEQ ID NO: 2, or equivalent positions in parent glucoamylases and particularly In a further embodiment, some variants may include the substitutions at positions: of SEQ ID NO: 2, or equivalent positions in parent glucoamylases and particularly In a further embodiment, some variants may include the substitutions at positions: of SEQ ID NO: 2, or equivalent positions in parent glucoamylases and particularly In a further embodiment, some variants may include the substitutions at positions: of SEQ ID NO: 2, or equivalent positions in parent glucoamylases and particularly In a further embodiment, some variants has the following substitutions: D44R/N61I/A539R or D44R/A539R of SEQ ID NO: 2. In a further embodiment, the variant comprises SEQ ID NO:1098. In yet a further embodiment, the variant consists of SEQ ID NO:1098. In a further embodiment, the variant comprises SEQ ID NO:1099. In yet a further embodiment, the variant consists of SEQ ID NO:1099. A number of parent glucoamylases have been aligned with the amino acid sequence of TrGA. In some embodiments, for example, the variant glucoamylase will be derived from a parent glucoamylase that is an The present disclosure also provides glucoamylase variants having at least one altered property (e.g., improved property) as compared to a parent glucoamylase and particularly to the TrGA. In some embodiments, at least one altered property (e.g., improved property) is selected from the group consisting of IS/SH-ratio, starch hydrolysis activity, real degree of fermentation, reduced formation of condensation products, acid stability, thermal stability and specific activity. Typically, the altered property is reduced IS/SH-ratio, enhanced real degree of fermentation, reduced formation of condensation products, increased thermal stability and/or increased specific activity. The increased thermal stability typically is at higher temperatures. In one embodiment, the increased pH stability is at high pH. In a further embodiment, the increased pH stability is at low pH. The glucoamylase variants of the disclosure may also provide higher rates of starch hydrolysis at low substrate concentrations as compared to the parent glucoamylase. The variant may have a higher Vmax or lower Km than a parent glucoamylase when tested under the same conditions. For example the variant glucoamylase may have a higher Vmax at a temperature range of about 25° C. to about 70° C. (e.g., about 25° C. to about 35° C.; about 30° C. to about 35° C.; about 40° C. to about 50° C.; at about 50° C. to about 55° C., or about 55° C. to about 62° C.). The Michaelis-Menten constant, Km and Vmax values can be easily determined using standard known procedures. In another aspect, the glucoamylase may also exhibit a reduced starch hydrolysis activity which is not more than 5%, not more than 10% or not more than 15% reduced as compared to the parent glucoamylase such as TrGA. In some aspects, the disclosure relates to a variant glucoamylase having altered thermal stability as compared to a parent (wild-type). Altered thermostability can be at increased temperatures or at decreased temperatures. Thermostability is measured as the % residual activity after incubation for 1 hour at 64° C. in NaAc buffer pH 4.5. Under these conditions, TrGA has a residual activity of between about 15% and 44% due to day-to-day variation as compared to the initial activity before incubation. Thus, in some embodiments, variants with increased thermostability have a residual activity that is between at least about 1% and at least about 50% more than that of the parent (after incubation for 1 hour at 64° C. in NaAc buffer pH 4.5), including about 2%, about 3%, about 4%, about 5%, about 6%, about 7%, about 8%, about 9%, about 10%, about 11%, about 12%, about 13%, about 14%, about 15%, about 16%, about 17%, about 18%, about 19%, about 20%, about 21%, about 22%, about 23%, about 24%, about 25%, about 26%, about 27%, about 28%, about 29%, about 30%, about 31%, about 32%, about 33%, about 34%, about 35%, about 36%, about 37%, about 38%, about 39%, about 40%, about 41%, about 42%, about 43%, about 44%, about 45%, about 46%, about 47%, about 48%, about 49%, and about 50% as compared to the initial activity before incubation. For example, when the parent residual activity is 15%, a variant with increased thermal stability may have a residual activity of between about 16% and about 75%. In some embodiments, the glucoamylase variant will have improved thermostability such as retaining at least about 50%, about 60%, about 70%, about 75%, about 80%, about 85%, about 90%, about 92%, about 95%, about 96%, about 97%, about 98%, or about 99% enzymatic activity after exposure to altered temperatures over a given time period, for example, at least about 60 minutes, about 120 minutes, about 180 minutes, about 240 minutes, or about 300 minutes. In some embodiments, the variant has increased thermal stability compared to the parent glucoamylase at selected temperatures in the range of about 40° C. to about 80° C., also in the range of about 50° C. to about 75° C., and in the range of about 60° C. to about 70° C., and at a pH range of about 4.0 to about 6.0. In some embodiments, the thermostability is determined as described in the Assays and Methods. That method may be adapted as appropriate to measure thermostability at other temperatures. Alternatively the thermostability may be determined at 64° C. as described there. In some embodiments, the variant has increased thermal stability at lower temperature compared to the parent glucoamylase at selected temperature in the range of about 20° C. to about 50° C., including about 35° C. to about 45° C. and about 30° C. to about 40° C. In some embodiments, variants having an improvement in thermostability include one or more deletions, substitutions or insertions and particularly substitutions in the following positions in the amino acid sequence set forth in SEQ ID NO: 2: 10, 42, 43, 44, 59, 61, 68, 72, 73, 97, 98, 99, 102, 114, 133, 140, 144, 152, 153, 182, 204, 205, 214, 216, 228, 229, 230, 231, 236, 241, 242, 263, 264, 265, 268, 269, 276, 284, 291, 294, 300, 301, 303, 311, 338, 342, 344, 346, 349, 359, 361, 364, 375, 379, 382, 390, 391, 393, 394, 410, 417, 430, 431, 433, 436, 442, 444, 448, 451, 493, 495, 503, 508, 511, 518, 519, 520, 527, 531, 535, 536, 537, 539, 563, or 577, or an equivalent position in a parent glucoamylase. In some embodiments, the parent glucoamylase will be a As used herein, specific activity is the activity of the glucoamylase per mg of protein. Activity was determined using the ethanol assay. The screening identified variants having a Performance Index (PI)>1.0 compared to the parent TrGA PI. The PI is calculated from the specific activities (activity/mg enzyme) of the wild-type (WT) and the variant enzymes. It is the quotient “Variant-specific activity/WT-specific activity” and can be a measure of the increase in specific activity of the variant. A PI of about 2 should be about 2 fold better than WT. In some aspects, the disclosure relates to a variant glucoamylase having altered specific activity as compared to a parent or wild-type glucoamylase. In some embodiments, the altered specific activity is increased specific activity. Increased specific activity can be defined as an increased performance index of greater than or equal to about 1, including greater than or equal to about 1.1, about 1.2, about 1.3, about 1.4, about 1.5, about 1.6, about 1.7, about 1.8, about 1.9, and about 2. In some embodiments, the increased specific activity is from about 1.0 to about 5.0, including about 1.1, about 1.2, about 1.3, about 1.4, about 1.5, about 1.6, about 1.7, about 1.8, about 1.9, about 2.0, about 2.1, about 2.2., about 2.3, about 2.4, about 2.5, about 2.6, about 2.7, about 2.8, about 2.9, about 3.0, about 3.1, about 3.2, about 3.3, about 3.4, about 3.5, about 3.6, about 3.7, about 3.8, about 3.9, about 4.0, about 4.1, about 4.2, about 4.3, about 4.4, about 4.5, about 4.6, about 4.7, about 4.8, and about 4.9. In some embodiments, the variant has an at least about 1.0 fold higher specific activity than the parent glucoamylase, including at least about 1.1 fold, about 1.2 fold, about 1.3 fold, about 1.4 fold, about 1.5 fold, about 1.6 fold, about 1.7 fold, about 1.8 fold, about 1.9 fold, about 2.0 fold, about 2.2 fold, about 2.5 fold, about 2.7 fold, about 2.9 fold, about 3.0 fold, about 4.0 fold, and about 5.0 fold. In some embodiments, variants having an improvement in specific activity include one or more deletions, substitutions or insertions in the following positions in the amino acid sequence set forth in SEQ ID NO: 2: 10, 14, 15, 23, 59, 60, 61, 65, 67, 68, 72, 73, 97, 98, 99, 102, 110, 113, 133, 140, 144, 145, 147, 152, 153, 164, 182, 204, 205, 214, 216, 219, 228, 229, 230, 231, 236, 239, 241, 242, 263, 264, 265, 268, 269, 276, 284, 291, 300, 301, 303, 311, 338, 342, 344, 346, 349, 359, 361, 364, 375, 379, 382, 390, 391, 393, 394, 410, 417, 418, 430, 431, 433, 442, 444, 448, 451, 493, 494, 495, 502, 503, 508, 511, 518, 519, 520, 531, 535, 536, 539, or 563, or an equivalent position in a parent glucoamylase. In some embodiments, the parent glucoamylase will comprise a sequence having at least about 50%, about 60%, about 70%, about 80%, about 90%, or about 95% sequence identity to the sequence of SEQ ID NO: 2. In some embodiments, the parent glucoamylase will also have structural identity to SEQ ID NO: 2. In some embodiments, variants of the disclosure having improved specific activity include a substitution in the following positions in the amino acid sequence set forth in SEQ ID NO: 2: I43Q, I43R, D44C, D44R, N061I, T067M, A072Y, S097N, S102A, S102M, S102R, I133T, N145I, N153D, T205Q, Q219S, W228A, W228F, W228H, W228M, S230C, S230F, 5230G, 5230L, 5230N, S230Q, S230R, S231L, I239V, I239Y, N263P, A268C, A268G, A268K, S291A, G294C, T342V, K394S, L417R, L417V, T430K, A431I, A431L, A431Q, R433Y, T451K, T495M, A519I, A520C, A520L, A520P, A535R, V536M, A539R, N563K, or N563I, or an equivalent position in a parent glucoamylase. In some embodiments, the specific activity of the parent as compared to the variant is determined as described in the Assays and Methods. In some aspects, the disclosure relates to a variant glucoamylase having both altered thermostability and altered specific activity as compared to a parent (e.g., wild-type). In some embodiments, the altered specific activity is an increased specific activity. In some embodiments, the altered thermostability is an increased thermostability at high temperatures (e.g., at temperatures above 80° C.) as compared to the parent glucoamylase. In some embodiments, variants with an increased thermostability and increased specific activity include one or more deletions, substitutions or insertions and substitutions in the following positions in the amino acid sequence set forth in SEQ ID NO: 2: 10, 15, 43, 44, 59, 61, 68, 72, 73, 97, 99, 102, 140, 153, 182, 204, 205, 214, 228, 229, 230, 231, 236, 241, 242, 264, 265, 268, 276, 284, 291, 294, 300, 301, 303, 311, 338, 344, 346, 349, 359, 361, 364, 375, 379, 382, 391, 393, 394, 410, 430, 433, 444, 448, 451, 495, 503, 511, 520, 531, 535, 536, 539, or 563, or an equivalent position in a parent glucoamylase. In some embodiments, the parent glucoamylase will be a In a further aspect, the glucoamylase exhibit an enhanced production of fermentable sugar(s) as compared to the parent glucoamylase such as TrGA. In a further aspect, the glucoamylase exhibit an enhanced production of fermentable sugars in the mashing step of the brewing process as compared to the parent glucoamylase such as TrGA. In a further aspect, the glucoamylase exhibit an enhanced production of fermentable sugars in the fermentation step of the brewing process as compared to the parent glucoamylase such as TrGA. In a further aspect, the fermentable sugar is glucose. A skilled person within the field can determine the production of fermentable sugar(s) by e.g. HPLC techniques. In a further aspect, the glucoamylase exhibit a reduced ratio between isomaltose synthesis and starch hydrolysis activity (IS/SH ratio) as compared to the parent glucoamylase such as TrGA. In a further aspect, the glucoamylase exhibit a starch hydrolysis activity which is not more than 5%, not more than 10% or not more than 15% reduced as compared to the parent glucoamylase such as TrGA. In one aspect, a screening method for identification of a glucoamylase variant having a reduced synthesis of condensation products during hydrolysis of starch and the glucoamylse variants obtained by the method is provided, the method comprising the steps of measuring the isomaltose synthesis and starch hydrolysis activity of glucoamylase variants and selecting the variants having a reduced starch hydrolysis activity which is not more than 5%, not more than 10% or not more than 15% reduced as compared to the parent glucoamylase and having a reduced ratio between isomaltose synthesis and starch hydrolysis activity (IS/SH ratio) as compared to the parent glucoamylase. In some embodiments the glucoamylase variants are selecting for having a reduced ratio between isomaltose synthesis and starch hydrolysis activity (IS/SH ratio) as compared to the parent glucoamylase. In some embodiments the glucoamylase variants are selecting for having the same or increased starch hydrolysis activity and reduced isomaltose synthesis, which is not more than 5%, not more than 10% or not more than 15% reduced as compared to the parent glucoamylase and thereby having a reduced ratio between isomaltose synthesis and starch hydrolysis activity (IS/SH ratio) as compared to the parent glucoamylase. In a further aspect, the glucoamylase exhibit an enhanced real degree of fermentation as compared to the parent glucoamylase such as TrGA. 5.6 Variant Glucoamylases with an Altered Formation of Condensation Products In one aspect, the glucoamylase forms a lower amount of condensation products than the amount of condensation products formed by The present disclosure also relates to isolated polynucleotides encoding the variant glucoamylase. The polynucleotides may be prepared by established techniques known in the art. The polynucleotides may be prepared synthetically, such as by an automatic DNA synthesizer. The DNA sequence may be of mixed genomic (or cDNA) and synthetic origin prepared by ligating fragments together. The polynucleotides may also be prepared by polymerase chain reaction (PCR) using specific primers. In general, reference is made to Minshull J. et al., The present disclosure also provides isolated polynucleotides comprising a nucleotide sequence (i) having at least about 50% identity to SEQ ID NO: 4, including at least about 60%, about 70%, about 80%, about 90%, about 95%, and about 99%, or (ii) being capable of hybridizing to a probe derived from the nucleotide sequence set forth in SEQ ID NO: 4, under conditions of intermediate to high stringency, or (iii) being complementary to a nucleotide sequence having at least 90% sequence identity to the sequence set forth in SEQ ID NO: 4. Probes useful according to the disclosure may include at least about 50, about 100, about 150, about 200, about 250, about 300 or more contiguous nucleotides of SEQ ID NO: 4. In some embodiments, the encoded polypeptide also has structural identity to SEQ ID NO: 2. The present disclosure further provides isolated polynucleotides that encode variant glucoamylases that comprise an amino acid sequence comprising at least about 50%, about 60%, about 70%, about 80%, about 90%, about 93%, about 95%, about 97%, about 98%, or about 99% amino acid sequence identity to SEQ ID NO: 2. Additionally, the present disclosure provides expression vectors comprising any of the polynucleotides provided above. The present disclosure also provides fragments (i.e., portions) of the DNA encoding the variant glucoamylases provided herein. These fragments find use in obtaining partial length DNA fragments capable of being used to isolate or identify polynucleotides encoding mature glucoamylase enzymes described herein from filamentous fungal cells (e.g., According to one embodiment of the disclosure, a DNA construct comprising a polynucleotide as described above encoding a variant glucoamylase encompassed by the disclosure and operably linked to a promoter sequence is assembled to transfer into a host cell. In one aspect, a polynucleotide encoding a glucoamylase variant as disclosed herein is provided. The DNA construct may be introduced into a host cell using a vector. In one aspect, a vector comprising the polynucleotide, or capable of expressing a glucoamylase variant as disclosed herein is provided. The vector may be any vector that when introduced into a host cell is stably introduced. In some embodiments, the vector is integrated into the host cell genome and is replicated. Vectors include cloning vectors, expression vectors, shuttle vectors, plasmids, phage particles, cassettes and the like. In some embodiments, the vector is an expression vector that comprises regulatory sequences operably linked to the glucoamylase coding sequence. Examples of suitable expression and/or integration vectors are provided in Sambrook et al. (1989) supra, and Ausubel (1987) supra, and van den Hondel et al. (1991) in Bennett and Lasure (Eds.) More Gene Manipulations In Fungi, Academic Press pp. 396-428 and U.S. Pat. No. 5,874,276. Reference is also made to the Fungal Genetics Stock Center Catalogue of Strains (FGSC, http://www.fgsc.net) for a list of vectors. Particularly useful vectors include vectors obtained from for example Invitrogen and Promega. Suitable plasmids for use in bacterial cells include pBR322 and pUC19 permitting replication in Specific vectors suitable for use in fungal cells include pRAX, a general purpose expression vector useful in In some embodiments, the promoter that shows transcriptional activity in a bacterial or a fungal host cell may be derived from genes encoding proteins either homologous or heterologous to the host cell. The promoter may be a mutant, a truncated and/or a hybrid promoter. The above-mentioned promoters are known in the art. Examples of suitable promoters useful in fungal cells and particularly filamentous fungal cells such as In some embodiments, the DNA construct includes nucleic acids coding for a signal sequence, that is, an amino acid sequence linked to the amino terminus of the polypeptide that directs the encoded polypeptide into the cell's secretory pathway. The 5′ end of the coding sequence of the nucleic acid sequence may naturally include a signal peptide coding region that is naturally linked in translation reading frame with the segment of the glucoamylase coding sequence that encodes the secreted glucoamylase or the 5′ end of the coding sequence of the nucleic acid sequence may include a signal peptide that is foreign to the coding sequence. In some embodiments, the DNA construct includes a signal sequence that is naturally associated with a parent glucoamylase gene from which a variant glucoamylase has been obtained. In some embodiments, the signal sequence will be the sequence depicted in SEQ ID NO: 1 or a sequence having at least about 90%, about 94, or about 98% sequence identity thereto. Effective signal sequences may include the signal sequences obtained from other filamentous fungal enzymes, such as from In additional embodiments, a DNA construct or vector comprising a signal sequence and a promoter sequence to be introduced into a host cell are derived from the same source. In some embodiments, the native glucoamylase signal sequence of a In some embodiments, the expression vector also includes a termination sequence. Any termination sequence functional in the host cell may be used in the present disclosure. In some embodiments, the termination sequence and the promoter sequence are derived from the same source. In another embodiment, the termination sequence is homologous to the host cell. Useful termination sequences include termination sequences obtained from the genes of In some embodiments, an expression vector includes a selectable marker. Examples of selectable markers include ones that confer antimicrobial resistance (e.g., hygromycin and phleomycin). Nutritional selective markers also find use in the present disclosure including those markers known in the art as amdS (acetamidase), argB (ornithine carbamoyltransferase) and pyrG (orotidine-5′ phosphate decarboxylase). Markers useful in vector systems for transformation of Methods used to ligate the DNA construct comprising a nucleic acid sequence encoding a variant glucoamylase, a promoter, a termination and other sequences and to insert them into a suitable vector are well known in the art. Linking is generally accomplished by ligation at convenient restriction sites. If such sites do not exist, synthetic oligonucleotide linkers are used in accordance with conventional practice (see Sambrook et al. (1989) supra, and Bennett and Lasure, More Gene Manipulations In Fungi, Academic Press, San Diego (1991) pp 70-76). Additionally, vectors can be constructed using known recombination techniques (e.g., Invitrogen Life Technologies, Gateway Technology). 1. The present disclosure also relates to host cells comprising a polynucleotide encoding a variant glucoamylase of the disclosure. In some embodiments, the host cells are chosen from bacterial, fungal, plant and yeast cells. The term host cell includes both the cells, progeny of the cells and protoplasts created from the cells that are used to produce a variant glucoamylase according to the disclosure. In one aspect, a host cell comprising, preferably transformed with a vector is disclosed. In a further aspect, a cell capable of expressing a glucoamylase variant is provided. In a further aspect, the host cell is a protease deficient and/or xylanase deficient and/or glucanase deficient host cell. A protease deficient and/or xylanase deficient and/or native glucanase deficient host cell may be obtained by deleting or silencing the genes coding for the mentioned enzymes. As a consequence the host cell containing the GA-variant is not expressing the mentioned enzymes In some embodiments, the host cells are fungal cells and optionally filamentous fungal host cells. The term “filamentous fungi” refers to all filamentous forms of the subdivision Eumycotina (see, Alexopoulos, C. J. (1962), Introductory Mycology, Wiley, New York). These fungi are characterized by a vegetative mycelium with a cell wall composed of chitin, cellulose, and other complex polysaccharides. The filamentous fungi of the present disclosure are morphologically, physiologically, and genetically distinct from yeasts. Vegetative growth by filamentous fungi is by hyphal elongation and carbon catabolism is obligatory aerobic. In the present disclosure, the filamentous fungal parent cell may be a cell of a species of, but not limited to, In some embodiments, the host cells will be gram-positive bacterial cells. Non-limiting examples include strains of In some embodiments, the host cell is a gram-negative bacterial strain, such as Introduction of a DNA construct or vector into a host cell includes techniques such as transformation; electroporation; nuclear microinjection; transduction; transfection, (e.g., lipofection-mediated and DEAE-Dextrin mediated transfection); incubation with calcium phosphate DNA precipitate; high velocity bombardment with DNA-coated microprojectiles; and protoplast fusion. General transformation techniques are known in the art (see, e.g., Ausubel et al. (1987) supra, chapter 9; and Sambrook et al. (1989) supra, and Campbell et al., Transformation methods for Transformation methods for In one specific embodiment, the preparation of In some embodiments, genetically stable transformants are constructed with vector systems whereby the nucleic acid encoding the variant glucoamylase is stably integrated into a host strain chromosome. Transformants are then purified by known techniques. In some further embodiments, the host cells are plant cells, such as cells from a monocot plant (e.g., corn, wheat, and sorghum) or cells from a dicot plant (e.g., soybean). Methods for making DNA constructs useful in transformation of plants and methods for plant transformation are known. Some of these methods include The present disclosure further relates to methods of producing the variant glucoamylases, which comprises transforming a host cell with an expression vector comprising a polynucleotide encoding a variant glucoamylase according to the disclosure, culturing the host cell under conditions suitable for expression and production of the variant glucoamylase and optionally recovering the variant glucoamylase. In one aspect, a method of expressing a variant glucoamylase according to the disclosure, the method comprising obtaining a host cell or a cell as disclosed herein and expressing the glucoamylase variant from the cell or host cell, and optionally purifying the glucoamylase variant, is provided. In one aspect, the glucoamylase variant is purified. In the expression and production methods of the present disclosure the host cells are cultured under suitable conditions in shake flask cultivation, small scale or large scale fermentations (including continuous, batch and fed batch fermentations) in laboratory or industrial fermentors, with suitable medium containing physiological salts and nutrients (see, e.g., Pourquie, J. et al., Biochemistry And Genetics Of Cellulose Degradation, eds. Aubert, J. P. et al., Academic Press, pp. 71-86, 1988 and Ilmen, M. et al., In some embodiments, the present disclosure relates to methods of producing the variant glucoamylase in a plant host comprising transforming a plant cell with a vector comprising a polynucleotide encoding a glucoamylase variant according to the disclosure and growing the plant cell under conditions suitable for the expression and production of the variant. In some embodiments, assays are carried out to evaluate the expression of a variant glucoamylase by a cell line that has been transformed with a polynucleotide encoding a variant glucoamylase encompassed by the disclosure. The assays can be carried out at the protein level, the RNA level and/or by use of functional bioassays particular to glucoamylase activity and/or production. Some of these assays include Northern blotting, dot blotting (DNA or RNA analysis), RT-PCR (reverse transcriptase polymerase chain reaction), in situ hybridization using an appropriately labeled probe (based on the nucleic acid coding sequence) and conventional Southern blotting and autoradiography. In addition, the production and/or expression of a variant glucoamylase may be measured in a sample directly, for example, by assays directly measuring reducing sugars such as glucose in the culture medium and by assays for measuring glucoamylase activity, expression and/or production. In particular, glucoamylase activity may be assayed by the 3,5-dinitrosalicylic acid (DNS) method (see Goto et al., The glucoamylases of the present disclosure may be recovered or purified from culture media by a variety of procedures known in the art including centrifugation, filtration, extraction, precipitation and the like. In one aspect, the use of a glucoamylase variant as described herein for the preparation of an enzymatic composition, is provided. The variant glucoamylases of the disclosure may be used in enzyme compositions including but not limited to starch hydrolyzing and saccharifying compositions, cleaning and detergent compositions (e.g., laundry detergents, dish washing detergents, and hard surface cleaning compositions), alcohol fermentation compositions, and in animal feed compositions. Further, the variant glucoamylases may be used in, for example, brewing, healthcare, textile, environmental waste conversion processes, biopulp processing, and biomass conversion applications. The variant glucoamylases of the disclosure may be used in enzyme compositions including a starch hydrolyzing composition, a saccharifying composition, a detergent, an alcohol fermentation enzymatic composition, and an animal feed. In one aspect, the composition is a starch hydrolyzing composition. In some embodiments, an enzyme composition comprising a variant glucoamylase encompassed by the disclosure will be optionally used in combination with any one or combination of the following enzymes—alpha-amylases, proteases, pullulanases, isoamylases, cellulases, hemicellulases, xylanases, cyclodextrin glycotransferases, lipases, phytases, laccases, oxidases, esterases, cutinases, xylanases, granular starch hydrolyzing enzymes and other glucoamylases. In some embodiments, an enzyme composition comprising a variant glucoamylase encompassed by the disclosure will be optionally used in combination with any one or combination of the following enzymes—amylase, protease, pullulanase, cellulase, glucanase, xylanase, arabinofuranosidase, ferulic acid esterase, xylan acetyl esterase and a further glucoamylase. In some embodiments, an enzyme composition comprising a variant glucoamylase encompassed by the disclosure will be optionally used in combination with any one or combination of the following enzymes—amylase, pullulanase and a further glucoamylase. In some embodiments, an enzyme composition comprising a variant glucoamylase encompassed by the disclosure will be optionally used in combination with any one or combination of the following enzymes—amylase and pullulanase. In a further aspect, the amylase is alpha-amylase and/or isoamylase. In a further aspect, the glucanase is exoglucanase and/or endoglucanase. In some embodiments, the enzyme composition will include an alpha-amylase such as fungal alpha-amylases (e.g., In some embodiments, the enzyme composition will include a pullulanase (EC 3.2.1.41). In one aspect, the pullulanases used herein is pullulanase from e.g. In other embodiments, the variant glucoamylases of the disclosure may be combined with other glucoamylases. In some embodiments, the glucoamylases of the disclosure will be combined with one or more glucoamylases derived from strains of In particular, the variant glucoamylases may be used for starch conversion processes, and particularly in the production of dextrose for fructose syrups, specialty sugars and in alcohol and other end-product (e.g., organic acid, ascorbic acid, and amino acids) production from fermentation of starch containing substrates (G. M. A. van Beynum et al., Eds. (1985) Starch Conversion Technology, Marcel Dekker Inc. NY). Dextrins produced using variant glucoamylase compositions of the disclosure may result in glucose yields of at least 80%, at least 85%, at least 90% and at least 95%. Production of alcohol from the fermentation of starch substrates using glucoamylases encompassed by the disclosure may include the production of fuel alcohol or portable alcohol. In some embodiments, the production of alcohol will be greater when the variant glucoamylase is used under the same conditions as the parent glucoamylase. In some embodiments, the production of alcohol will be between about 0.5% and 2.5% better, including but not limited to about 0.6%, about 0.7%, about 0.8%, about 0.9%, about 1.0%, about 1.1%, about 1.2%, about 1.3%, about 1.4%, about 1.5%, about 1.6%. about 1.7%, about 1.8%, about 1.9%, about 2.0%, about 2.1%, about 2.2%, about 2.3%, and about 2.4% more alcohol than the parent glucoamylase. In some embodiments, the variant glucoamylases of the disclosure will find use in the hydrolysis of starch from various plant-based substrates, which are used for alcohol production. In some embodiments, the plant-based substrates will include corn, wheat, barley, rye, milo, rice, sugar cane, potatoes and combinations thereof. In some embodiments, the plant-based substrate will be fractionated plant material, for example a cereal grain such as corn, which is fractionated into components such as fiber, germ, protein and starch (endosperm) (U.S. Pat. No. 6,254,914 and U.S. Pat. No. 6,899,910). Methods of alcohol fermentations are described in The Alcohol Textbook, K. A. Jacques et al., Eds. 2003, Nottingham University Press, UK. In certain embodiments, the alcohol will be ethanol. In particular, alcohol fermentation production processes are characterized as wet milling or dry milling processes. In some embodiments, the variant glucoamylase will be used in a wet milling fermentation process and in other embodiments the variant glucoamylase will find use in a dry milling process. Dry grain milling involves a number of basic steps, which generally include: grinding, cooking, liquefaction, saccharification, fermentation and separation of liquid and solids to produce alcohol and other co-products. Plant material and particularly whole cereal grains, such as corn, wheat or rye are ground. In some cases, the grain may be first fractionated into component parts. The ground plant material may be milled to obtain a coarse or fine particle. The ground plant material is mixed with liquid (e.g., water and/or thin stillage) in a slurry tank. The slurry is subjected to high temperatures (e.g., about 90° C. to about 105° C. or higher) in a jet cooker along with liquefying enzymes (e.g., alpha-amylases) to solublize and hydrolyze the starch in the grain to dextrins. The mixture is cooled down and further treated with saccharifying enzymes, such as glucoamylases encompassed by the instant disclosure, to produce glucose. The mash containing glucose may then be fermented for approximately 24 to 120 hours in the presence of fermentation microorganisms, such as ethanol producing microorganism and particularly yeast ( In some embodiments, the saccharification step and fermentation step are combined and the process is referred to as simultaneous saccharification and fermentation or simultaneous saccharification, yeast propagation and fermentation. In other embodiments, the variant glucoamylase is used in a process for starch hydrolysis wherein the temperature of the process is between about 30° C. and about 75° C., in some embodiments, between about 40° C. and about 65° C. In some embodiments, the variant glucoamylase is used in a process for starch hydrolysis at a pH between about 3.0 and about 6.5. The fermentation processes in some embodiments include milling of a cereal grain or fractionated grain and combining the ground cereal grain with liquid to form a slurry that is then mixed in a single vessel with a variant glucoamylase according to the disclosure and optionally other enzymes such as, but not limited to, alpha-amylases, other glucoamylases, phytases, proteases, pullulanases, isoamylases or other enzymes having granular starch hydrolyzing activity and yeast to produce ethanol and other co-products (see e.g., U.S. Pat. No. 4,514,496, WO 04/081193, and WO 04/080923). In some embodiments, the disclosure pertains to a method of saccharifying a liquid starch solution, which comprises an enzymatic saccharification step using a variant glucoamylase of the disclosure. The liquid starch solution may be produced by solubilising starch in water or an aqueous buffer and optionally heating to gelatinize the starch. Further partial degradation of the starch by amylases may be applied. The present invention provides a method of using glucoamylase variants of the invention for producing glucose and the like from starch. Generally, the method includes the steps of partially hydrolyzing precursor starch in the presence of alpha-amylase and then further hydrolyzing the release of D-glucose from the non-reducing ends of the starch or related oligo- and polysaccharide molecules in the presence of glucoamylase by cleaving alpha-(1-4) and alpha-(1-6) glucosidic bonds. The partial hydrolysis of the precursor starch utilizing alpha-amylase provides an initial breakdown of the starch molecules by hydrolyzing internal alpha-(1-4)-linkages. In commercial applications, the initial hydrolysis using alpha-amylase is run at a temperature of approximately 105° C. A very high starch concentration is processed, usually 30% to 40% solids. The initial hydrolysis is usually carried out for five minutes at this elevated temperature. The partially hydrolyzed starch can then be transferred to a second tank and incubated for approximately one hour at a temperature of 85° to 90° C. to derive a dextrose equivalent (D.E.) of 10 to 15. The step of further hydrolyzing the release of D-glucose from the non-reducing ends of the starch or related oligo- and polysaccharides molecules in the presence of glucoamylase is normally carried out in a separate tank at a reduced temperature between 30° and 60° C. Often the temperature of the substrate liquid is dropped to between 55° C. and 60° C. The pH of the solution is dropped from 6 to 6.5 to a range between 3 and 5.5. Often, the pH of the solution is 4 to 4.5. The glucoamylase is added to the solution and the reaction is carried out for 24-72 hours, such as 36-48 hours. Examples of saccharification processes wherein the glucoamylase variants of the invention may be used include the processes described in JP 3-224493; JP 1-191693; JP 62-272987; and EP 452,238. The glucoamylase variant(s) described herein may be used in combination with an enzyme that hydrolyzes only alpha-(1-6)-glucosidic bonds in molecules with at least four glucosyl residues. Preferentially, the glucoamylase variant can be used in combination with pullulanase or alpha-amylase. The use of alpha-amylase and pullulanase for debranching, the molecular properties of the enzymes, and the potential use of the enzymes with glucoamylase is set forth in G. M. A. van Beynum et al., In one embodiment, the use of a glucoamylase variant as described herein in a starch conversion process, such as in a continuous saccharification step, is provided. The glucoamylase variants described herein may also be used in immobilised form. This is suitable and often used for producing maltodextrins or glucose syrups or speciality syrups, such as maltose syrups and further for the raffinate stream of oligosaccharides in connection with the production of fructose syrups. When the desired final sugar product is, e.g., high fructose syrup the dextrose syrup may be converted into fructose. After the saccharification process the pH is increased to a value in the range of 6-8, such as pH 7.5, and the calcium is removed by ion exchange. The dextrose syrup is then converted into high fructose syrup using, e.g., an immobilized glucose isomerase (such as Sweetzyme™ IT). In other embodiments, the variant glucoamylase is used in a process for beer brewing. Brewing processes are well-known in the art, and generally involve the steps of malting, mashing, and fermentation. Mashing is the process of converting starch from the milled barley malt and solid adjuncts into fermentable and un-fermentable sugars to produce wort. Traditional mashing involves mixing milled barley malt and adjuncts with water at a set temperature and volume to continue the biochemical changes initiated during the malting process. The mashing process is conducted over a period of time at various temperatures in order to activate the endogenous enzymes responsible for the degradation of proteins and carbohydrates. After mashing, the wort is separated from the solids (spent grains). Following wort separation, the wort may be fermented with brewers' yeast to produce a beer. The short-branched glucose oligomers formed during mashing may be further hydrolyzed by addition of exogenous enzymes like glucoamylases and/or alpha-amylases, beta-amylases and pullulanase, among others. The wort may be used as it is or it may be concentrated and/or dried. The concentrated and/or dried wort may be used as brewing extract, as malt extract flavoring, for non-alcoholic malt beverages, malt vinegar, breakfast cereals, for confectionary etc. The wort is fermented to produce an alcoholic beverage, typically a beer, e.g., ale, strong ale, bitter, stout, porter, lager, export beer, malt liquor, barley wine, happoushu, high-alcohol beer, low-alcohol beer, low-calorie beer, or light beer. In another typical embodiment, the wort is fermented to produce portable ethanol. In some embodiments, the disclosure pertains to a method of hydrolyzing and saccharifying gelatinised and liquefied (typically) grist starch to be used in brewing, whereby an enzymatic composition comprising one or more glucoamylases as contemplated herein, is used to enhance the amount of brewers' yeast fermentable sugars obtained from the starch. A brewing process is used to produce the portable product, beer, where fermentable sugars are converted to ethanol and CO2 by fermentation with brewers' yeast. The fermentable sugars are traditionally derived from starch in cereal grains, optionally supplemented with fermentable sugar sources such as glucose and maltose syrups and cane sugar. Briefly, beer production, well-known in the art, typically includes the steps of malting, mashing, and fermentation. Historically the first step in beer production is malting—steeping, germination and drying of cereal grain (e.g. barley). During malting enzymes are produced in the germinating cereal (e.g. barley) kernel and there are certain changes in its chemical constituents (known as modification) including some degradation of starch, proteins and beta-glucans. The malted cereal is milled to give a grist which may be mixed with a milled adjunct (e.g. non-germinated cereal grain) to give a mixed grist. The grist is mixed with water and subjected to mashing; a previously cooked (gelatinised and liquefied) adjunct may be added to the mash. The mashing process is conducted over a period of time at various temperatures in order to hydrolyse cereal proteins, degrade beta-glucans and solubilise and hydrolyse the starch. The hydrolysis of the grist starch in the malt and adjunct in traditional mashing is catalysed by two main enzymes endogenous to malted barley. Alpha-amylase, randomly cleaves alpha-1,4 bonds in the interior of the starch molecule fragmenting them into smaller dextrins. Beta-amylase sequentially cleaves alpha-1,4 bonds from the non-reducing end of the these dextrins producing mainly maltose. Both alpha- and beta-amylase are unable to hydrolyse the alpha-1,6 bonds which forms the branching points of the starch chains in the starch molecule, which results in the accumulation of limit dextrins in the mash. Malt does contain an enzyme, limit dextrinase, which catalyses the hydrolysis of alpha-1,6 bonds but it only shows weak activity at mashing temperatures due to its thermolability. After mashing, the liquid extract (wort) is separated from the spent grain solids (i.e. the insoluble grain and husk material forming part of grist). The objectives of wort separation include: —to obtain good extract recovery, —to obtain good filterability, and—to produce clear wort. Extract recovery and filterability of the wort are important in the economics of the brewing process. The composition of the wort depends on the raw materials, mashing process and profiles and other variables. A typical wort comprises 65-80% fermentable sugars (glucose, maltose and maltotriose, and 20-35% non-fermentable limit dextrins (sugars with a higher degree of polymerization than maltotriose). An insufficiency of starch hydrolytic enzymes during mashing can arise when brewing with high levels of adjunct unmalted cereal grists. A source of exogenous enzymes, capable of producing fermentable sugars during the mashing process is thus needed. Furthermore, such exogenous enzymes are also needed to reduce the level of non-fermentable sugars in the wort, with a corresponding increase in fermentable sugars, in order to brew highly attenuated beers with a low carbohydrate content. Herein disclosed is a enzyme composition for hydrolysis of starch comprising at least one glucoamylase as contemplated herein, which can be added to the mash or used in the mashing step of a brewing process, in order to cleave alpha-1,4 bonds and/or alpha-1,6 bonds in starch grist and thereby increase the fermentable sugar content of the wort and reduce the residue of non-fermentable sugars in the finished beer. In addition, the wort, so produced may be dried (by for example spray drying) or concentrated (e.g. boiling and evaporation) to provide a syrup or powder. The grist, as contemplated herein, may comprise any starch and/or sugar containing plant material derivable from any plant and plant part, including tubers, roots, stems, leaves and seeds. Often the grist comprises grain, such as grain from barley, wheat, rye, oat, corn, rice, milo, millet and sorghum, and more preferably, at least 10%, or more preferably at least 15%, even more preferably at least 25%, or most preferably at least 35%, such as at least 50%, at least 75%, at least 90% or even 100% (w/w) of the grist of the wort is derived from grain. Most preferably the grist comprises malted grain, such as barley malt. Preferably, at least 10%, or more preferably at least 15%, even more preferably at least 25%, or most preferably at least 35%, such as at least 50%, at least 75%, at least 90% or even 100% (w/w) of the grist of the wort is derived from malted grain. Preferably the grist comprises adjunct, such as non-malted grain from barley, wheat, rye, oat, corn, rice, milo, millet and sorghum, and more preferably, at least 10%, or more preferably at least 15%, even more preferably at least 25%, or most preferably at least 35%, such as at least 50%, at least 75%, at least 90% or even 100% (w/w) of the grist of the wort is derived from non-malted grain or other adjunct. Adjunct comprising readily fermentable carbohydrates such as sugars or syrups may be added to the malt mash before, during or after the mashing process of the invention but is preferably added after the mashing process. A part of the adjunct may be treated with an alpha-amylase, and/or endopeptidase (protease) and/or a endoglucanase, and/or heat treated before being added to the mash. The enzyme composition, as contemplated herein, may include additional enzyme(s), preferably an enzyme selected from among an alpha-amylase, protease, pullulanase, isoamylase, cellulase, glucanase such as exoglucanase or endoglucanase, xylanase, arabinofuranosidase, feruloyl esterase, xylan acetyl esterase, phytase and glucoamylase. During the mashing process, starch extracted from the grist is gradually hydrolyzed into fermentable sugars and smaller dextrins. Preferably the mash is starch negative to iodine testing, before wort separation. In one aspect, a pullulanase (E. C. 3.2.1.41) enzyme activity is exogenously supplied and present in the mash. The pullulanase may be added to the mash ingredients, e.g., the water and/or the grist before, during or after forming the mash. In another aspect, an alpha-amylase enzyme activity is exogenously supplied and present in the mash. The alpha-amylase may be added to the mash ingredients, e.g., the water and/or the grist before, during or after forming the mash. In a further aspect, both pullulanase and alpha-amylase enzyme activities are exogenously supplied and present in the mash. The alpha-amylase and pullulanase may be added to the mash ingredients, e.g., the water and/or the grist before, during or after forming the mash. A further enzyme may be added to the mash, said enzyme being selected from the group consisting of among amylase, protease, pullulanase, isoamylase, cellulase, glucanase, xylanase, arabinofuranosidase, ferulic acid esterase, xylan acetyl esterase, phytase and a further glucoamylase. Prior to the third step of the brewing process, fermentation, the wort is typically transferred to a brew kettle and boiled vigorously for 50-60 minutes. A number of important processes occur during wort boiling (further information may be found in “Technology Brewing and Malting” by Wolfgang Kunze of the Research and Teaching Institute of Brewing, Berlin (VLB), 3rd completely updated edition, 2004, ISBN 3-921690-49-8) including inactivation of the endogenous malt enzymes and any exogenous enzyme added to the mash or adjunct. The boiled wort is then cooled, pitched with brewers' yeast and fermented at temperatures typically ranging from 8-16° C. to convert the fermentable sugars to ethanol. A low-alcohol beer can be produced from the final beer, by a process of vacuum evaporation that serves to selectively remove alcohol. In an alternative embodiment, the disclosure pertains to a method of enhancing the amount of fermentable sugars in the wort, using an enzymatic composition comprising one or more glucoamylases as contemplated herein (e.g. thermolabile glucoamylase), whereby the enzymatic composition is added to the wort after it has been boiled, such that the one or more glucoamylases are active during the fermentation step. The enzymatic composition can be added to the boiled wort either before, simultaneously, or after the wort is pitched with the brewers' yeast. At the end of the fermentation and maturation step the beer, which may optionally be subjected to vacuum evaporation to produce a low-alcohol beer, is then pasteurized. An inherent advantage of this method lies in the duration of the fermentation process, which is about 6-15 days (depending on pitching rate, fermentation, temperature, etc), which allows more time for the enzymatic cleavage of non-fermentable sugars, as compared to the short mashing step (2-4 h duration). A further advantage of this method lies in the amount of the enzymatic composition needed to achieve the desired decrease in non-fermentable sugars (and increase in fermentable sugars), which corresponds to a significantly lower number of units of enzymatic activity (e.g. units of glucoamylase activity) than would need to be added to the mash to achieve a similar decrease in non-fermentable sugars. In addition, it removes the difficulties often seen during wort separation, especially by lautering, when high dose rates of glucoamylase are added in the mash. In one aspect, the disclosure pertains to an enzymatic composition comprising at least one additional enzyme selected among amylase, protease, pullulanase, isoamylase, cellulase, glucanase, xylanase, arabinofuranosidase, ferulic acid esterase, xylan acetyl esterase, phytase and a further glucoamylase. In a further aspect, the disclosure pertains to an enzymatic composition, wherein the composition comprises at least one additional enzyme selected among alpha-amylase and/or pullulanase. In a further aspect, the disclosure pertains to an enzymatic composition, wherein the composition further comprises alpha-amylase and pullulanase. In a further aspect, the disclosure pertains to an enzymatic composition, which enzymatic composition comprises less than 1, less than 0.8, less than 0.6, less than 0.5, less than 0.4, less than 0.2, less than 0.125, less than 0.1, less than 0.05, less than 0.01, or less than 0.005 XU of xylanase activity per GAU of a glucoamylase variant as described herein. If desired, xylanase activity may be reduced by different methods known to the skilled person such as e.g. heat treatment, passing through wheat bran, or other materials, which may selectively adsorb xylanase activity. In a further aspect, the disclosure pertains to an enzymatic composition, which enzymatic composition comprises less than 400, less than 200, less than 50, less than 20, or less than 2 XU of xylanase activity per gram of the composition. In a further aspect, the disclosure pertains to an enzymatic composition, which enzymatic composition comprises between 0.1-20, 0.1-10, 0.1-5 or 0.2-3 SSU of alpha-amylase activity per GAU of a glucoamylase variant as described herein. In a further aspect, the disclosure pertains to an enzymatic composition, which enzymatic composition comprises between 0.30-10, 1-8, 3-10 or 5-9 PU of pullulanase activity per GAU of a glucoamylase variant as described herein. In a further aspect, the disclosure pertains to an enzymatic composition, which enzymatic composition comprises between 0.95-20 SSU of alpha-amylase activity per GAU of a glucoamylase variant as described herein and between 0.30-10 PU of pullulanase activity per GAU of a glucoamylase variant as described herein. In a further aspect, the disclosure pertains to an enzymatic composition, which enzymatic composition comprises between 0.95-20 SSU of alpha-amylase activity per GAU of a glucoamylase variant as described herein and between 0.30-10 PU of pullulanase activity per GAU of a glucoamylase variant as described herein and less than 1, less than 0.8, less than 0.6, less than 0.5, less than 0.4, less than 0.2, less than 0.125, less than 0.1, less than 0.05, less than 0.01, or less than 0.005 XU of xylanase activity per GAU of a glucoamylase variant as described herein. In a further aspect, the disclosure pertains to an enzymatic composition, which enzymatic composition comprises between 0.05-10, 0.1-10, 0.1-8, 0.1-5, 0.1-3, 0.2-3, 0.2-2 PU of pullulanase activity per GAU of a glucoamylase variant as described herein. In a further aspect, the disclosure pertains to an enzymatic composition, which enzymatic composition comprises between 0.1-20, 1-15, 2-10, 3-10 SSU of alpha-amylase activity per GAU of a glucoamylase variant as described herein. In a further aspect, the disclosure pertains to an enzymatic composition, which enzymatic composition comprises between 0.05-10 PU of pullulanase activity per GAU of a glucoamylase variant as described herein and between 0.1-20 SSU of alpha-amylase activity per GAU of a glucoamylase variant as described herein. In a further aspect, the disclosure pertains to an enzymatic composition, which enzymatic composition comprises between 0.1-5 PU of pullulanase activity per GAU of a glucoamylase variant as described herein and between 1-15 SSU of alpha-amylase activity per GAU of a glucoamylase variant as described herein. In a further aspect, the disclosure pertains to an enzymatic composition, which enzymatic composition comprises between 0.2-2 PU of pullulanase activity per GAU of a glucoamylase variant as described herein and between 2-10 SSU of alpha-amylase activity per GAU of a glucoamylase variant as described herein. In a further aspect, the disclosure pertains to an enzymatic composition, which enzymatic composition comprises between 0.05-10 PU of pullulanase activity per GAU of a glucoamylase variant as described herein and between 0.1-20 SSU of alpha-amylase activity per GAU of a glucoamylase variant as described herein and less than 1, less than 0.8, less than 0.6, less than 0.5, less than 0.4, less than 0.2, less than 0.125, less than 0.1, less than 0.05, less than 0.01, or less than 0.005 XU of xylanase activity per GAU of a glucoamylase variant as described herein. In a further aspect, the disclosure pertains to an enzymatic composition, which enzymatic composition comprises between 0.1-5 PU of pullulanase activity per GAU of a glucoamylase variant as described herein and between 1-15 SSU of alpha-amylase activity per GAU of a glucoamylase variant as described herein and less than 1, less than 0.8, less than 0.6, less than 0.5, less than 0.4, less than 0.2, less than 0.125, less than 0.1, less than 0.05, less than 0.01, or less than 0.005 XU of xylanase activity per GAU of a glucoamylase variant as described herein. In a further aspect, the disclosure pertains to an enzymatic composition, which enzymatic composition comprises between 0.2-2 PU of pullulanase activity per GAU of a glucoamylase variant as described herein and between 2-10 SSU of alpha-amylase activity per GAU of a glucoamylase variant as described herein and less than 1, less than 0.8, less than 0.6, less than 0.5, less than 0.4, less than 0.2, less than 0.125, less than 0.1, less than 0.05, less than 0.01, or less than 0.005 XU of xylanase activity per GAU of a glucoamylase variant as described herein. In one aspect, the glucoamylase variant as described herein is added in an amount of 500-20000 GAU/kg grist. In another aspect, the glucoamylase variant as described herein is added in an amount of 750-10000 GAU/kg grist. In a further aspect, the glucoamylase variant as described herein is added in an amount of 1000-7500 GAU/kg grist. The present disclosure also provides an animal feed composition or formulation comprising at least one variant glucoamylase encompassed by the disclosure. Methods of using a glucoamylase enzyme in the production of feeds comprising starch are provided in WO 03/049550 (herein incorporated by reference in its entirety). Briefly, the glucoamylase variant is admixed with a feed comprising starch. The glucoamylase is capable of degrading resistant starch for use by the animal. In some embodiments a glucoamylase variant as described herein is used in processes in the generation of fuels based on starch feed stocks. Other objects and advantages of the present disclosure are apparent from the present specification. Further embodiments according to the invention: Use of a glucoamylase variant comprising two or more amino acid substitutions relative to interconnecting loop 2′ with the amino acid sequence from position 518 to position 543 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or loop 1 with the amino acid sequence from position 21 to position 51 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or helix 2 with the amino acid sequence from position 52 to position 68 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or loop 11 with the amino acid sequence from position 396 to position 420 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase, and/or helix 12 with the amino acid sequence from position 421 to position 434 of SEQ ID NO:2 or equivalent sequence of residues in a parent glucoamylase for reducing the synthesis of condensation products during hydrolysis of starch. Use of a glucoamylase variant, which when in its crystal, form has a crystal structure for which the atomic coordinates of the main chain atoms have a root-mean-square deviation from the atomic coordinates of the equivalent main chain atoms of TrGA (as defined in Table 20 in WO2009/067218) of less than 0.13 nm following alignment of equivalent main chain atoms, and which have a linker region, a starch binding domain and a catalytic domain, said variant comprising two or more amino acid substitutions relative to the amino acid sequence of the parent glucoamylase in interconnecting loop 2′ of the starch binding domain, and/or in loop 1, and/or in helix 2, and/or in loop 11, and/or in helix 12 of the catalytic domain for reducing the synthesis of condensation products during hydrolysis of starch. The use of a glucoamylase variant according to any one of the embodiments 1-2, wherein said two or more amino acid substitutions are relative to the interconnecting loop 2′ with the amino acid sequence from position 518 to position 543 of SEQ ID NO:2, and/or loop 1 with the amino acid sequence from position 21 to position 51 of SEQ ID NO:2, and/or helix 2 with the amino acid sequence from position 52 to position 68 of SEQ ID NO:2, and/or loop 11 with the amino acid sequence from position 396 to position 420 of SEQ ID NO:2, and/or helix 12 with the amino acid sequence from position 421 to position 434 of SEQ ID NO:2. The use of a glucoamylase variant according to any one of the embodiments 1-3, wherein the two or more amino acid substitutions are at least one amino acid substitution in the interconnecting loop 2′ and at least one amino acid substitution in loop 1 and/or helix 2 and/or loop 11 and/or helix 12. The use of a glucoamylase variant according to any one of the embodiments 1-4, wherein the two or more amino acid substitutions are 1, 2, 3 or 4 amino acid substitutions in the interconnecting loop 2′ and 1, 2, 3 or 4 amino acid substitutions in loop 1 and/or helix 2 and/or loop 11 and/or helix 12. The use of a glucoamylase variant according to any one of the embodiments 1-5, wherein the two or more amino acid substitutions are at least one amino acid substitution in interconnecting loop 2′ and at least one amino acid substitution in loop 1. The use of a glucoamylase variant according to any one of the embodiments 1-6, wherein the two or more amino acid substitutions are at least one amino acid substitution in interconnecting loop 2′ and at least one amino acid substitution in helix 2. The use of a glucoamylase variant according to any one of the embodiments 1-7, wherein the two or more amino acid substitutions are at least one amino acid substitution in interconnecting loop 2′ and at least one amino acid substitution in loop 11. The use of a glucoamylase variant according to any one of the embodiments 1-8, wherein the two or more amino acid substitutions are at least one amino acid substitution in interconnecting loop 2′ and at least one amino acid substitution in helix 12. The use of a glucoamylase variant according to any one of the embodiments 1-9, wherein the two or more amino acid substitutions are at least one amino acid substitution in interconnecting loop 2′ and at least one amino acid substitution in loop 1 and at least one amino acid substitution in helix 2. The use of a glucoamylase variant according to any one of embodiments 1-10, wherein the glucoamylase variant has at least one amino acid substitution within position 520-543, 530-543, or 534-543 of interconnecting loop 2′, the positions corresponding to the respective position in SEQ ID NO:2 or equivalent positions in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-11, wherein the glucoamylase variant has at least one amino acid substitution within the amino acid sequence of position 30-50, 35-48, or 40-46 of loop 1, the positions corresponding to the respective position in SEQ ID NO:2 or equivalent positions in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-12, wherein the glucoamylase variant has at least one amino acid substitution within the amino acid sequence of position 50-66, 55-64, or 58-63 of helix 2, the positions corresponding to the respective position in SEQ ID NO:2 or equivalent positions in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-13, wherein the glucoamylase variant has at least one amino acid substitution within the amino acid sequence of position 405-420, 410-420, or 415-420 of loop 11, the positions corresponding to the respective position in SEQ ID NO:2 or equivalent positions in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-14, wherein the glucoamylase variant has at least one amino acid substitution within the amino acid sequence of position 421-434, 425-434, or 428-434 of helix 12, the positions corresponding to the respective position in SEQ ID NO:2 or equivalent positions in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-15, wherein the glucoamylase variant has at least 80%, 85%, 90%, 95%, 98%, or 99.5% sequence identity to the parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-16, wherein the glucoamylase variant has at least 80%, 85%, 90%, 9S %, 98%, or 99.5% sequence identity to SEQ ID NO: 1, 2, 3, 5, 6, 7, 8, or 9. The use of a glucoamylase variant to any one of the embodiments 1-17, wherein the glucoamylase variant has a starch binding domain that has at least 96%, 97%, 98%, 99%, or 99.5% sequence identity with the starch binding domain of SEQ ID NO: 1, 2, 11, 385, 386, 387, 388, 389, or 390. The use of a glucoamylase variant according to any one of the embodiments 1-18, wherein the glucoamylase variant has a catalytic domain that has at least 80%, 85%, 90%, 95%, or 99.5% sequence identity with the catalytic domain of SEQ ID NO: 1, 2, 3, 5, 6, 7, 8, or 9. The use of a glucoamylase variant according to any one of embodiments 1-19, wherein the glucoamylase variant has at least 80%, 85%, 90%, 95%, 98%, or 99.5% sequence identity to SEQ ID NO:2. The use of a glucoamylase variant according to any one of embodiments 1-20, wherein the condensation product is isomaltose. The use of a glucoamylase variant according to any one of embodiments 1-21, wherein the hydrolysis of starch is in a brewing process. The use of a glucoamylase variant according to any one of embodiments 1-22, wherein the glucoamylase exhibit an enhanced production of fermentable sugar(s) as compared to the parent glucoamylase, such as TrGA. The use of a glucoamylase variant according to any one of embodiments 1-23, wherein the glucoamylase exhibit an enhanced production of fermentable sugars in a mashing step of the brewing process as compared to the parent glucoamylase, such as TrGA. The use of a glucoamylase variant according to any one of embodiments 1-24, wherein the glucoamylase exhibit an enhanced production of fermentable sugars in a fermentation step of the brewing process as compared to the parent glucoamylase, such as TrGA. The use of a glucoamylase variant according to any one of embodiments 1-25, wherein the fermentable sugar is glucose. The use of a glucoamylase variant according to any one of embodiments 1-26, wherein the hydrolysis of starch is in a process for producing glucose syrup. The use of a glucoamylase variant according to any one of embodiments 1-27, wherein the glucoamylase exhibit a reduced ratio between isomaltose synthesis (IS) and starch hydrolysis activity (SH) as compared to the parent glucoamylase, such as TrGA. The use of a glucoamylase variant according to any one of embodiments 1-28, wherein the glucoamylase exhibit a reduced starch hydrolysis activity, which is not more than 5%, not more than 10% or not more than 15% reduced as compared to the parent glucoamylase, such as TrGA. The use of a glucoamylase variant according to any one of embodiments 1-29, wherein the glucoamylase exhibit an enhanced real degree of fermentation as compared to the parent glucoamylase such as TrGA. The use of a glucoamylase variant according to any one of embodiments 1-30, wherein the glucoamylase forms a lower amount of condensation products than the amount of condensation products formed by the glucoamylase The use of a glucoamylase variant according to any one of embodiments 1-31, wherein the glucoamylase forms an amount of condensation products which amount is essentially the same as, not more than 5% higher, not more than 8% higher or not more than 10% higher than the amount of condensation products formed by The use of a glucoamylase variant according to any one of embodiments 31-32, wherein dosing of the glucoamylases are the same based on protein concentration. The use of a glucoamylase variant according to any one of embodiments 31-33, wherein dosing of the glucoamylases are the same based on measurement of activity in activity assays. The use of a glucoamylase variant according to any one of embodiments 1-34, which glucoamylase variant has an amino acid substitution in position 539 and one or more amino acid substitutions in a position selected from position 44, 61, 417 and 431, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-35, which glucoamylase variant has an amino acid substitution in position 539 and a) an amino acid substitution in position 44 and/or b) amino acid substitutions in both positions 417 and 431, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-36, which glucoamylase variant has an amino acid substitution in position 539 and an amino acid substitution in position 44, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-37, which glucoamylase variant has an amino acid substitution in position 539 and amino acid substitutions in positions 417 and 431, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-38, which glucoamylase variant has an amino acid substitution in position 539 and amino acid substitutions in positions 44 and 61, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-39, which glucoamylase variant has an amino acid substitution in position 43, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-40, which glucoamylase variant has an amino acid substitution in position 61, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-41, wherein the amino acid substitution in position 539 is 539R, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-42, wherein the amino acid substitution in position 44 is 44R, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-43, wherein the amino acid substitution in position 417 is 417R/V, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-44, wherein the amino acid substitution in position 417 is 417R, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-45, wherein the amino acid substitution in position 417 is 417V, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-46, wherein the amino acid substitution in position 431 is 431L, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-47, wherein the amino acid substitution in position 43 is 43R, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The use of a glucoamylase variant according to any one of embodiments 1-48, wherein the amino acid substitution in position 61 is 61I, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. A glucoamylase variant as defined in any one of embodiments 1-49. A glucoamylase variant comprising two or more amino acid substitutions, wherein an amino acid substitution is in position 539 and an amino acid substitution is in position 44, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase, and which sequence has at least 80% sequence identity to the parent glucoamylase, and wherein the amino acid substitution in position 44 is not 44C. The glucoamylase variant according to embodiment 51 comprising two or more amino acid substitutions, wherein an amino acid substitution is in position 539 and an amino acid substitution is 44R, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The glucoamylase variant according to any one of embodiments 51-52 comprising an amino acid substitution in position 61, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The glucoamylase variant according to any one of embodiments 51-53, wherein the glucoamylase variant has at least 85%, 90%, 95%, 98%, or 99.5% sequence identity to the parent glucoamylase. The glucoamylase variant according to any one of embodiments 51-54, wherein the glucoamylase variant has at least 85%, 90%, 95%, 98%, or 99.5% sequence identity to SEQ ID NO: 1, 2, 3, 5, 6, 7, 8, or 9. The glucoamylase variant according to any one of embodiments 51-55, wherein the glucoamylase variant has at least 85%, 90%, 95%, 98%, or 99.5% sequence identity to SEQ ID NO:2. The glucoamylase variant according to any one of embodiments 51-56, wherein the amino acid substitution in position 539 is 539R, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The glucoamylase variant according to any one of embodiments 51-57, wherein the amino acid substitution in position 44 is 44R, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The glucoamylase variant according to any one of embodiments 51-58, wherein the amino acid substitution in position 61 is 61I, the position corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase. The glucoamylase variant according to any one of embodiments 51-59 comprising the following amino acid substitutions:
The glucoamylase variant according to any one of embodiments 51-60 consisting of SEQ ID NO:2 and having the following amino acid substitutions:
The glucoamylase variant according to any one of embodiments 51-61, wherein the glucoamylase variant has a starch binding domain that has at least 96%, 97%, 98%, 99%, or 99.5% sequence identity with the starch binding domain of SEQ ID NO: 1, 2, 11, 385, 386, 387, 388, 389, or 390. The glucoamylase variant according to any one of embodiments 51-62, wherein the glucoamylase variant has a catalytic domain that has at least 80%, 85%, 90%, 95%, or 99.5% sequence identity with the catalytic domain of SEQ ID NO: 1, 2, 3, 5, 6, 7, 8, or 9. The glucoamylase variant according to any one of embodiments 50-63, wherein the parent glucoamylase is selected from a glucoamylase obtained from a The glucoamylase variant according to any one of embodiments 50-64, wherein the parent glucoamylase is obtained from a The glucoamylase variant according to any one of embodiments 50-65, which glucoamylase exhibit an enhanced production of fermentable sugar(s) as compared to the parent glucoamylase such as TrGA. The glucoamylase variant according to any one of embodiments 50-66, which glucoamylase exhibit an enhanced production of fermentable sugars in the mashing step of the brewing process as compared to the parent glucoamylase such as TrGA. The glucoamylase variant according to any one of embodiments 50-67, which glucoamylase exhibit an enhanced production of fermentable sugars in the fermentation step of the brewing process as compared to the parent glucoamylase such as TrGA. The glucoamylase variant according to embodiment 68, wherein the fermentable sugar is glucose. The glucoamylase variant according to any one of embodiments 50-69, which glucoamylase exhibit a reduced ratio between isomaltose synthesis and starch hydrolysis activity (IS/SH ratio) as compared to the parent glucoamylase such as TrGA. The glucoamylase variant according to any one of embodiments 50-70, which glucoamylase exhibit a reduced starch hydrolysis activity which is not more than 5%, not more than 10% or not more than 15% reduced as compared to the parent glucoamylase such as TrGA. The glucoamylase variant according to any one of embodiments 50-71, which glucoamylase exhibit an enhanced real degree of fermentation as compared to the parent glucoamylase such as TrGA. The glucoamylase variant according to any one of embodiments 50-72, which glucoamylase forms a lower amount of condensation products than the amount of condensation products formed by The glucoamylase variant according to any one of embodiments 50-73, which glucoamylase forms an amount of condensation products which amount is essentially the same as, not more than 5%, not more than 8%, or not more than 10% higher than the amount of condensation products formed by The glucoamylase variant according to any one of embodiments 73-74, wherein the dosing of the glucoamylases are the same based on protein concentration. The glucoamylase variant according to any one of embodiments 73-74, wherein the dosing of the glucoamylases are the same based on measurement of activity in activity assays. The glucoamylase variant according to any one of embodiments 50-76, which glucoamylase has been purified. A polynucleotide encoding a glucoamylase variant according to any of embodiments 50-77. A vector comprising the polynucleotide according to embodiment 78, or capable of expressing a glucoamylase variant according to any of embodiments 50-77. A host cell comprising a vector according to embodiment 79. A host cell which has stably integrated into the chromosome a nucleic acid encoding the variant glucoamylase according to any of embodiments 50-80. A cell capable of expressing a glucoamylase variant according to any one of embodiments 50-76. The host cell according to any one of embodiments 78-81, or the cell according to embodiment 81, which is a bacterial, fungal or yeast cell. The host cell according to embodiment 83, which is The host cell according to any one of embodiments 83-84, which is a protease deficient and/or xylanase deficient and/or native glucanase deficient host cell. A method of expressing a glucoamylase variant, the method comprising obtaining a host cell or a cell according to any one of embodiments 80-85 and expressing the glucoamylase variant from the cell or host cell, and optionally purifying the glucoamylase variant. The method according to embodiment 86 comprising purifying the glucoamylase variant. Use of a glucoamylase variant according to any one of embodiments 50-76 for the preparation of an enzymatic composition. An enzymatic composition comprising at least one glucoamylase variant according to any one of embodiments 50-77. The enzymatic composition according to embodiment 89 comprising at least one glucoamylase variant according to any one of embodiments 50-77, wherein the composition is selected from among a starch hydrolyzing composition, a saccharifying composition, a detergent, an alcohol fermentation enzymatic composition, and an animal feed. The enzymatic composition according to embodiment 90, which is a starch hydrolyzing composition. The enzymatic composition according to any one of embodiments 89-91 comprising at least one additional enzyme selected among amylase, protease, pullulanase, cellulase, glucanase, xylanase, arabinofuranosidase, ferulic acid esterase, xylan acetyl esterase, and a further glucoamylase. The enzymatic composition according to embodiment 89-92, wherein the at least one additional enzyme is selected among amylase, pullulanase, and a further glucoamylase. The enzymatic composition according to embodiment 89-93, wherein the at least one additional is selected among amylase and pullulanase. The enzymatic composition according to any one of embodiments 89-94, wherein the amylase is selected among alpha-amylase, and isoamylase. A method for converting starch or partially hydrolyzed starch into a syrup containing glucose, said process including saccharifying a liquid starch solution in the presence of at least one glucoamylase variant according to any one of embodiments 50-77 or an enzymatic composition according to any one of embodiments 89-95. The method according to embodiment 96 of saccharifying a liquid starch solution, which comprises an enzymatic saccharification step using a glucoamylase variant according to embodiment 50-77 or an enzymatic composition according to any one of embodiments 89-95. The method according to any one of embodiments 96-97, further comprising contacting the liquid starch solution with at least one additional enzyme. The method according to embodiment 98, wherein the additional enzyme is selected among amylase, protease, pullulanase, cellulase, glucanase, xylanase, arabinofuranosidase, ferulic acid esterase, xylan acetyl esterase, and glucoamylase. The method according to embodiment any one of embodiments 96-100, wherein the amylase is selected among alpha-amylase, and isoamylase. Use of a glucoamylase variant according to any one of embodiments 50-77 in a starch conversion process, such as a in a continuous starch conversion process. Use of a glucoamylase variant according to any one of embodiments 50-77 in a process for producing oligosaccharides, maltodextrins, or glucose syrups. Use of a glucoamylase variant according to any one of embodiments 50-77 in a process for producing high fructose corn syrup. A method for producing a wort for brewing comprising forming a mash from a grist, and contacting the mash with a glucoamylase variant according to any one of embodiments 50-77 or an enzymatic composition according to any one of embodiments 89-95. The method of embodiment 105, further comprising contacting the mash with one or more additional enzyme(s) The method according to embodiment 106, wherein the one or more enzyme(s) is selected among amylase, protease, pullulanase, cellulase, endoglucanase, xylanase, arabinofuranosidase, ferulic acid esterase, xylan acetyl esterase, and glucoamylase. The method according to embodiment 107, wherein the one or more enzyme(s) is amylase and/or pullulanase. The method according to embodiment any one of embodiments 107-108, wherein the amylase is alpha-amylase and/or isoamylase. The method according to any one of embodiments 105-109, wherein the grist comprises one or more of malted grain, unmalted grain, adjunct, and any combination thereof. The method of any one of embodiments 105-110, further comprising fermenting the wort to obtain a fermented beverage. The method of any one of embodiments 105-111, further comprising fermenting the wort to obtain a beer. A method for production of a beer which comprises:
The method of embodiment 113, wherein the beer is subjected to a pasteurization step. Use of a glucoamylase variant according to any one of embodiments 50-77 to enhance the production of fermentable sugars in either the mashing step or the fermentation step of a brewing process. A beer, wherein the beer is produced by the steps of:
d. pasteurizing the beer, wherein a glucoamylase variant according to any one of embodiments 50-77 is added to: step (a) and/or step (b) and/or step (c). The beer of embodiment 116, wherein the pasteurized beer is further characterized as being:
Use of a glucoamylase variant according to any one of embodiments 50-77 in an alcohol fermentation process. A screening method for identification of a glucoamylase variant having a reduced ratio between isomaltose synthesis and starch hydrolysis activity (IS/SH ratio) as compared to the parent glucoamylase. A screening method for identification of a glucoamylase variant having the same or increased starch hydrolysis activity and reduced isomaltose synthesis, which is not more than 5%, not more than 10% or not more than 15% reduced as compared to the parent glucoamylase and having a reduced ratio between isomaltose synthesis and starch hydrolysis activity (IS/SH ratio) as compared to the parent glucoamylase. A screening method for identification of a glucoamylase variant having a reduced synthesis of condensation products during hydrolysis of starch, the method comprising the steps of measuring the isomaltose synthesis and starch hydrolysis activity of glucoamylase variants and selecting the variants having a reduced starch hydrolysis activity which is not more than 5%, not more than 10% or not more than 15% reduced as compared to the parent glucoamylase and having a reduced ratio between isomaltose synthesis and starch hydrolysis activity (IS/SH ratio) as compared to the parent glucoamylase. The glucoamylase variant obtained by the method according to any one of embodiments 119-121. Further embodiments also part of the invention: A glucoamylase variant comprising the following amino acid substitutions:
The glucoamylase variant according to further embodiment 1 comprising the following amino acid substitutions:
The glucoamylase variant according to any one of further embodiments 1-2 comprising the following amino acid substitutions:
The glucoamylase variant according to any one of further embodiments 1-2 comprising the following amino acid substitutions:
The glucoamylase variant of any one of further embodiments 1-4, wherein the glucoamylase variant has at least 85% or 90% sequence identity with SEQ ID NO: 1 or 2. The glucoamylase variant of further embodiment 5, wherein the glucoamylase variant has at least 95% sequence identity with SEQ ID NO: 1 or 2. The glucoamylase variant of further embodiment 6, wherein the glucoamylase variant has at least 99.5% sequence identity with SEQ ID NO: 1 or 2. The glucoamylase variant of any one of further embodiments 1-7, wherein the parent glucoamylase comprises SEQ ID NO: 1 or 2. The glucoamylase variant of further embodiment 8, wherein the parent glucoamylase consists of SEQ ID NO: 1 or 2. The glucoamylase variant according to any one of further embodiments 1-9, wherein the glucoamylase variant has a starch binding domain that has at least 96%, 97%, 98%, 99%, or 99.5% sequence identity with the starch binding domain of SEQ ID NO: 1, 2, 11, 385, 386, 387, 388, 389, or 390. The glucoamylase variant according to any one of further embodiments 1-10, wherein the glucoamylase variant has a catalytic domain that has at least 80%, 85%, 90%, 95%, or 99.5% sequence identity with the catalytic domain of SEQ ID NO: 1, 2, 3, 5, 6, 7, 8, or 9. The glucoamylase variant according to any one of further embodiments 1-11, wherein the parent glucoamylase is selected from a glucoamylase obtained from a The glucoamylase variant according to any one of further embodiments 1-12, wherein the parent glucoamylase is obtained from a The glucoamylase variant according to any one of further embodiments 1-13, which glucoamylase exhibit an enhanced production of fermentable sugar(s) as compared to the parent glucoamylase. The glucoamylase variant according to any one of further embodiments 1-14, which glucoamylase exhibit an enhanced production of fermentable sugars in the mashing step of the brewing process as compared to the parent glucoamylase. The glucoamylase variant according to any one of further embodiments 1-15, which glucoamylase exhibit an enhanced production of fermentable sugars in the fermentation step of the brewing process as compared to the parent glucoamylase. The glucoamylase variant according to further embodiment 16, wherein the fermentable sugar is glucose. The glucoamylase variant according to any one of further embodiments 1-17, which glucoamylase exhibit a reduced ratio between isomaltose synthesis and starch hydrolysis activity (IS/SH ratio) as compared to the parent glucoamylase. The glucoamylase variant according to any one of further embodiments 1-18, which glucoamylase exhibit a reduced starch hydrolysis activity which is not more than 5%, not more than 10% or not more than 15% reduced as compared to the parent glucoamylase. The glucoamylase variant according to any one of further embodiments 1-19, which glucoamylase exhibit an enhanced real degree of fermentation as compared to the parent glucoamylase. The glucoamylase variant according to any one of further embodiments 1-20, which glucoamylase forms a lower amount of condensation products than the amount of condensation products formed by The glucoamylase variant according to any one of further embodiments 1-21, which glucoamylase forms an amount of condensation products which amount is essentially the same as, not more than 5%, not more than 8%, or not more than 10% higher than the amount of condensation products formed by The glucoamylase variant according to any one of further embodiments 18-21, wherein the dosing of the glucoamylases are the same based on protein concentration. The glucoamylase variant according to any one of further embodiments 18-23, wherein the dosing of the glucoamylases are the same based on measurement of activity in activity assays. The glucoamylase variant according to any one of further embodiments 1-24, which glucoamylase has been purified. A polynucleotide encoding a glucoamylase variant according to any of further embodiments 1-25. A vector comprising the polynucleotide according to further embodiment 26, or capable of expressing a glucoamylase variant according to any of further embodiments 1-25. A host cell comprising a vector according to further embodiment 27. A host cell which has stably integrated into the chromosome a nucleic acid encoding the variant glucoamylase according to any of further embodiments 1-25. A cell capable of expressing a glucoamylase variant according to any one of further embodiments 1-25. The host cell according to any one of further embodiments 28-29, or the cell according to further embodiment 30, which is a bacterial, fungal or yeast cell. The host cell according to further embodiment 31, which is The host cell according to any one of further embodiments 28-29 and 31-32, which is a protease deficient and/or xylanase deficient and/or glucanase deficient host cell. A method of expressing a glucoamylase variant, the method comprising obtaining a host cell or a cell according to any one of further embodiments 28-33 and expressing the glucoamylase variant from the cell or host cell, and optionally purifying the glucoamylase variant. The method according to further embodiment 34 comprising purifying the glucoamylase variant. Use of a glucoamylase variant according to any one of further embodiments 1-25 for the preparation of an enzymatic composition. An enzymatic composition comprising at least one glucoamylase variant according to any one of further embodiments 1-25. An enzymatic composition comprising at least one glucoamylase variant according to any one of embodiments 1-25, said enzyme composition comprising one or more further enzymes. The enzymatic composition according to any one of further embodiments 37-38 comprising at least one glucoamylase variant according to any one of further embodiments 1-25, wherein the composition is selected from among a starch hydrolyzing composition, a saccharifying composition, a detergent composition, an alcohol fermentation enzymatic composition, and an animal feed composition. An enzymatic composition according to any one of further embodiments 36-39 comprising at least one additional enzyme selected among amylase, protease, pullulanase, isoamylase, cellulase, glucanase, xylanase, arabinofuranosidase, ferulic acid esterase, xylan acetyl esterase, phytase and a further glucoamylase. The enzymatic composition according to any one of further embodiments 36-40, wherein the composition comprises at least one additional enzyme selected among alpha-amylase and/or pullulanase. The enzymatic composition according to any one of further embodiments 36-41, wherein the composition comprises alpha-amylase and pullulanase. The enzymatic composition according to any one of further embodiments 36-42, which enzymatic composition comprises less than 1, less than 0.8, less than 0.6, less than 0.5, less than 0.4, less than 0.2, less than 0.125, less than 0.1, less than 0.05, less than 0.01, or less than 0.005 XU of xylanase activity per GAU of a glucoamylase variant according to any one of further embodiments 1-25. The enzymatic composition according to any one of further embodiments 36-43, which enzymatic composition comprises less than 400, less than 200, less than 50, less than 20, or less than 2 XU of xylanase activity per gram of the composition. The enzymatic composition according to any one of further embodiments 36-44, which enzymatic composition comprises between 0.1-20, 1-15, 2-10, or 3-10 SSU of alpha-amylase activity per GAU of a glucoamylase variant according to any one of further embodiments 1-25. The enzymatic composition according to any one of further embodiments 36-45, which enzymatic composition comprises between 0.05-10, 0.1-10, 0.1-8, 0.1-5, 0.1-3, 0.2-3, or 0.2-2 PU of pullulanase activity per GAU of a glucoamylase variant according to any one of further embodiments 1-25. The enzymatic composition according to any one of further embodiments 36-46, which enzymatic composition comprises between 0.05-10 PU of pullulanase activity per GAU of a glucoamylase variant according to any one of further embodiments 1-25 and between 0.1-20 SSU of alpha-amylase activity per GAU of a glucoamylase variant according to any one of further embodiments 1-25. The enzymatic composition according to any one of further embodiments 36-47, which enzymatic composition comprises between 0.05-10 PU of pullulanase activity per GAU of a glucoamylase variant according to any one of further embodiments 1-25 and between 0.1-20 SSU of alpha-amylase activity per GAU of a glucoamylase variant according to any one of further embodiments 1-25 and less than 1, less than 0.8, less than 0.6, less than 0.5, less than 0.4, less than 0.2, less than 0.125, less than 0.1, less than 0.05, less than 0.01, or less than 0.005 XU of xylanase activity per GAU of a glucoamylase according to any one of further embodiments 1-25. A method for producing a wort for brewing comprising forming a mash from a grist, and contacting the mash with a glucoamylase variant according to any one of further embodiments 1-25 or an enzymatic composition according to any one of further embodiments 36-48. The method of further embodiment 49, further comprising contacting the mash with one or more additional enzyme(s) The method according to further embodiment 50, wherein the one or more enzyme(s) is selected among amylase, protease, pullulanase, isoamylase, cellulase, endoglucanase, xylanase, arabinofuranosidase, ferulic acid esterase, xylan acetyl esterase, phytase and glucoamylase. The method according to further embodiment 51, wherein the one or more enzyme(s) is/are alpha-amylase and/or pullulanase. The method according to any one of further embodiments 49-52, wherein the grist comprises one or more of malted grain, unmalted grain, adjunct, and any combination thereof. The method of any one of further embodiments 49-53, further comprising fermenting the wort to obtain a fermented beverage. The method of any one of further embodiments 49-54, further comprising fermenting the wort to obtain a beer. A method for production of a beer which comprises:
The method of further embodiment 55, wherein the beer is subjected to a pasteurization step. Use of a glucoamylase variant according to any one of further embodiments 1-25 or an enzymatic composition according to any one of further embodiments 36-48 to enhance the production of fermentable sugars in either the mashing step or the fermentation step of a brewing process. A beer, wherein the beer is produced by the steps of:
d. pasteurizing the beer, e. wherein a glucoamylase variant according to any one of further embodiments 1-25 or an enzymatic composition according to any one of further embodiments 36-48 is added to: step (a) and/or step (b) and/or step (c). The beer of further embodiment 59, wherein the pasteurized beer is further characterized as being:
The invention will now be further described by way of the following non-limiting examples. The following assays and methods are used in the examples provided below. The methods used to provide variants are described below. However, it should be noted that different methods may be used to provide variants of a parent enzyme and the invention is not limited to the methods used in the examples. It is intended that any suitable means for making variants and selection of variants may be used. pNPG Glucoamylase Activity Assay for 96-Well Microtiter Plates The reagent solutions were: NaAc buffer: 200 mM sodium acetate buffer pH 4.5; Substrate: 50 mM p-nitrophenyl-α-D-glucopyranoside (Sigma N-1377) in NaAc buffer (0.3 g/20 ml) and stop solution: 800 mM glycine-NaOH buffer pH 10. 30 μl filtered supernatant was placed in a fresh 96-well flat bottom micro titer plate (MTP). To each well 50 μl NaAc buffer and 120 μl substrate was added and incubated for 30 minutes at 50° C. (Thermolab systems iEMS Incubator/shaker HT). The reaction was terminated by adding 100 μl stop solution. The absorbance was measured at 405 nm in a MTP-reader (Molecular Devices Spectramax 384 plus) and the activity was calculated using a molar extinction coefficient of 0.011 μM/cm. With a stock dilution of 150 ppm of purified enzyme (in 50 mM NaAc pH 4.0), a 3 ppm dilution was made by adding 6 μl to 294 μl 50 mM NaAc buffer pH 4.5. The diluted sample was equally divided over 2 MTPs. One MTP (initial plate) was incubated for 1 hr at 4° C. and the other MTP (residual plate) was incubated at 64° C. (Thermolab systems iEMS Incubator/Shaker HT) for 1 hr. The residual plate was chilled for 10 min on ice. 60 μl of both the initial plate and the residual plate was added to 120 μl 4% soluble corn starch pH 3.7 and incubated for 2 hrs at 32° C., 900 rpm in 2 separate MTPs (Thermolabsystems iEMS Incubator/Shaker HT). Activity of both plates was measured in the Hexokinase activity assay, using the ethanol application assay described below. Thermal stability was calculated as % residual activity as follows: Hexokinase cocktail: 10-15 minutes prior to use, 90 ml water was added to a BoatIL container glucose HK R1 (IL test glucose (HK) kit, Instrument Laboratory #182507-40) and gently mixed. 100 μl of Hexokinase cocktail was added to 85 μl of dH2O. 15 μl of sample was added to the mixtures and incubated for 10 minutes in the dark at room temperature. Absorbance was read at 340 nm in a MTP-reader after 10 minutes. Glucose concentrations were calculated according to a glucose (0-1.6 mg/ml) standard curve. Ethanol Application—Glucose Release from Corn Starch 8% stock solution: 8 g of soluble corn starch (Sigma #S4180) was suspended in 40 ml dH2O at room temperature. The slurry was added in portions to 50 ml of boiling dH2O in a 250 ml flask and cooked for 5 minutes. The starch solution was cooled to 25° C. while stirring and the volume adjusted with remain 10 ml of dH2O. Stop solution: 800 mM Glycine-NaOH buffer, pH 10. 4% (m/v) soluble starch working solution: stock solution was diluted (1:1) with 100 mM sodium acetate buffer pH 4.0. 6 μl of 150 ppm purified enzyme was diluted with 294 μl 50 mM NaAc buffer pH 4.0 in a flat bottom 96-well MTP. 60 μl of this dilution was added to 120 μl 4% soluble corn starch pH 4.0 and incubated for 2 hrs at 32° C. 900 rpm (Thermolabsystems iEMS Incubator/Shaker HT). The reaction was stopped by adding 90 μl 4° C.—cold Stop Solution. The sample was placed on ice for 20 minutes. Starch was spun down at 1118×g at 10° C. for 5 minutes (SIGMA 6K15) and 15 μl supernatant was used in the Hexokinase activity assay described above to determine the glucose content. Protein levels were measured using a microfluidic electrophoresis instrument (Caliper Life Sciences, Hopkinton, Mass., USA). The microfluidic chip and protein samples were prepared according to the manufacturer's instructions (LabChip® HT Protein Express, P/N 760301). Culture supernatants were prepared and stored in 96-well microtiter plates at −20° C. until use, when they were thawed by warming in a 37° C. incubator for 30 minutes. After shaking briefly, 2 μl of each culture sample was transferred to a 96-well PCR plate (Bio-Rad, Hercules, Calif., USA) containing 7 μl samples buffer (Caliper) followed by heating the plate to 90° C. for 5 minutes on a thermostatically controlled plate heater. The plate was allowed to cool before adding 40 μl water to each sample. The plate was then placed in the instrument along with a protein standard supplied and calibrated by the manufacturer. As the proteins move past a focal point in the chip, the fluorescence signal is recorded and the protein concentration is determined by quantitating the signal relative to the signal generated by the calibrated set of protein standards. After the Caliper protein determination the data is processed in the following way. The calibration ladders are checked for correctness of the peak pattern. If the calibration ladder that is associated with the run does not suffice, it is replaced by a calibration ladder of an adjacent run. For peak detection, the default settings of the global peak find option of the caliper software are used. The peak of interest is selected at 75 kDA+/−10%. The result is exported to a spreadsheet program and the peak area is related to the corresponding activity (ABS340-blank measurement) in the ethanol screening assay. With the area and activity numbers of 12 Wild Type samples, a calibration line is made using the “Enzyme Kinetics” equation of the program Grafit Version 5 (Erithacus Software, Horley, UK) in combination with a non-linear fit function. The default settings are used to calculate the Km and Vmax parameters. Based on these two parameters, a Michaelis-Menten reference line is made and the specific activity of each variant is calculated. Based on the specific activity the performance index (PI) is calculated. The PI of a variant is the quotient “Variant-specific activity/WT-specific activity.” The PI of WT is 1.0 and a variant with a PI>1.0 has a specific activity that is greater than WT. Culture supernatants of expressed TrGA variants were purified in one step by affinity chromatography using an AKTA explorer 100 FPLC system (Amersham Biosciences, Piscataway, N.J.). β-cyclodextrin (Sigma-Aldrich, Zwijndrecht, The Netherlands; 85.608-8) was coupled to epoxy activated Sepharose beads (GE Healthcare, Diegem, Belgium; 17-0480-01) and employed for purification. The column was equilibrated with 25 mM sodium acetate buffer pH 4.3 followed by application of concentrated enzyme sample. Bound variants were eluted from the column with 25 mM sodium acetate buffer pH 4.3 containing 10 mM α-cyclodextrin (Sigma, 28705). Purified samples were analyzed using sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE). The protein concentration of purified TrGA variants was determined by anion exchange chromatography using an AKTA explorer 100 FPLC system. Purified sample was injected onto a ResourceQ—1 ml column (GE Healthcare) and a linear gradient of 0 to 500 mM NaCl in 25 mM sodium acetate buffer pH 4.3 was applied to elute bound protein. The peak area was determined and the protein concentration was calculated relative to a TrGA standard with know concentration. Glucose release of the variants was determined on corn mash liquefact from a local ethanol producer in a 6-well plate. Each well of the plate was filled with 6 g of 26% DS liquefact pH 4.3. Subsequently, 300 ppm enzyme and 400 ppm urea was added and 250 μl sample was collected after 2, 4 and 6 hr incubation at 32° C. The sample was centrifuged for 5 minutes at 14.000×g and 50 μl of the supernatant was transferred to an eppendorf tube containing 50 μl of kill solution (1.1 N sulfuric acid) and allowed to stand for 5 minutes. 250 μl of water was added to the tube and then filtered with a 0.22 μm filter plate and injected onto an HPX-87H column as described below. A sample of corn mash liquefact from a local ethanol producer was obtained and diluted in some cases to 26% DS using thin stillage. The pH of the slurry was adjusted to pH 4.3 using 4 N sulfuric acid. A 100 g or 50 g aliquot of mash was put into a 125 ml shake flask and placed into a 32° C. incubator and allowed to equilibrate. After addition of 100 μl 400 ppm urea, 1 ml purified variant at intended concentration or purified TrGA at 2 different concentrations was added to the shake flasks. Finally, 333 μl of a solution of Red Star Red yeast (15 g hydrated for 30 minutes in 45 ml DI water; Lesaffre yeast Corp. Milwaukee, Wis.) was added to each sample; Samples were collected at 5, 21, 28, 48 and 52 hours and analyzed by HPLC (Agilent 1200 series) using an Aminex HPX-87H column (Bio-Rad). A 2 ml eppendorf centrifuge tube was filled with fermentor beer and cooled on ice for 10 minutes. The sample was centrifuged for 3 minutes at 14.000×g and 500 μl of the supernatant was transferred to a test tube containing 50 μl of kill solution (1.1 N sulfuric acid) and allowed to stand for 5 minutes. 5.0 ml of water was added to the test tube and then filtered into a 0.22 μm filter plate (multiscreen, Millipore, Amsterdam, the Netherlands) and run on HPLC. Column Temperature: 60° C.; mobile phase: 0.01 N sulfuric acid; flow rate 0.6 ml/min; detector: R1; injection volume: 20 μl. The column separates molecules based on charge and molecular weight; DP1 (monosaccharides); DP2 (disaccharides); DP3 (trisaccharides); DP>3 (oligosaccharides sugars having a degree of polymerization greater than 3); succinic acid; lactic acid; glycerol; methanol; ethanol. Substrate: p-Nitrophenyl-β-maltoside (4 mM), plus thermostable β-glucosidase (5 U/ml) (from assay R-AMGR305/04; Megazyme International Wicklow, Ireland) was freshly prepared Buffer: 200 mM Sodium acetate buffer (pH 4.5). Enzyme samples were diluted by at least a factor 10 in sodium acetate buffer In a 96 well plate: 20 μl substrate was mixed with 20 μL enzyme solution and incubate at 40° C. with agitation for 10 minutes. 300 μL 2% Trizma base was added to terminate reaction and develop the colour. Absorbance at 400 nm was measured against a reagent blank. Blanks were prepared by adding 300 tit of Trizma base solution (2%) to 20 μL of substrate with vigorous stirring, followed by the enzyme solution (20 μL). Activity was calculated as follows: Where: GAU=International units of enzyme activity. One Unit is the amount of enzyme which release one μmole of p-nitrophenol from the substrate per minute at the defined pH and temperature. ΔA400=absorbance (reaction)−Absorbance (blank). 10=incubation time (min). 340=final reaction volume (μL). 20=volume of enzyme assayed (μL) 18.1=EmM p-nitrophenol in 2% trizma base (pH˜8.5) at 400 nm (unit: μM−1*cm−1). 0.88=Light path (cm) Buffer: 0.1 M Citrate buffer pH 5.4 (made from 0.1 M citric acid and 0.1 M Tri-sodium citrate) Substrate: 30% soluble starch (Merck, v.nr 1.01257.1000) in buffer (heat slightly until all starch is in solution) Enzyme: Glucoamylase standardised to 3 GAU/ml on basis of above assay. 60 μL 30% starch was transferred to a 96 well PCR plate. 60 μL enzyme sample or standard was added and mixed by pumping a couple of times with the pipette. Following steps until incubation was carried not as fast as possible. The PCR plate was covered with sealing tape and following PCR programme was run: 6 min at 63° C., 6 min at 99° C. and 10 min at 4° C. Lid was not heated. After the temperature cycle the PCR plate was centrifuged (app 1 min at 300 rpm) to collect all liquid in the bottom of the wells. Plates were stored at 4° C. until further analysis. Glucose concentration was measured according to method below and the hydrolysis activity was calculated as follows: Same as for starch hydrolysis activity except that substrate is 2% iso-maltose (Sigma 17253) and the first step in the PCR programme is 10 min at 63° C. instead of 6 min. Modified from the Megazyme© D-glucose assay (KGLUC 04/06) and used to determine the amount of glucose released from starch and isomaltose hydrolysis reactions. The contents of bottle 1 [Reagent Buffer: Potassium phosphate buffer (1.0 M, pH 7.4), p-hydroxybenzoic acid (0.22 M) and sodium azide (0.4% w/v)] was diluted to 1 L with distilled water. The contents of bottle 2 [Reagent Enzymes: Glucose oxidase (>12,000 U) plus peroxidase (>650 U) and 4-aminoantipyrine (80 mg). Freeze-dried powder] was diluted in approx. 20 mL of solution 1 and quantitatively transferred to the bottle containing the remainder of solution 1. This is Glucose Determination Reagent (GOPOD Reagent). It was either used fresh or stored frozen and dark. Before use it was cheked that the absorbance (A510) of this solution was less than 0.05 when read against distilled water. In a 96 well plate, add 250 μL of GOPOD reagent to 10 μL of sample solution. Cover the plate with sealing tape and incubate in an Eppendorf thermomixer at 40° C., 700 rpm for 20 min. Read absorbances at 510 nm. A glucose standard curve is made from solutions of 1.4; 1.2; 0.8; 0.4; 0.2 and 0 mg/ml glucose in milli-q water and used for calculation of the sample glucose concentrations. Substrate: 30% glucose in 0.1M citric acid buffer, pH 5.4 (heated slightly to bring all glucose into solution). Enzyme: Glucoamylase standardized to 3 GAU/ml Reference: Heat inactivated enzyme sample and/or buffer solution (not used in all cases). Standards: 1) 0.3% Maltose and 0.1% isomaltose in demineralised water. 2) 0.2% Maltose and 0.05% isomaltose in demineralised water. 3) 0.3% Maltose and 0.1% isomaltose in demineralised water. Reaction conditions: 60 μl substrate was mixed with 60 μL enzyme solution in wells of a PCR-plate. The plate with was covered with sealing tape and following temperature was run: 120 min at 63° C., 6 min at 99° C., 10 min at 4° C. Lid heated to 70° C. After incubation the plates were giveen a moderate centrifugation (1 min at 300 rpm), and they were store at 4° C. until further analysis. All samples were run in duplicate. Quantification of Maltose and Iso-Maltose: Preheat TLC-Plate at 167° C. for 10 min prior to sample application. Dilute all samples and standards 20 times in demineralised water. An automatic TLC sampler (ATS4, CAMAG, Muttenz, Switzerland) was used for accurately transferring 4 μL samples to the TLC plate. Each plate could contain 20 samples, placed in 4 mm wide bands. Plates were heated for 10 min at 40° C. to let bands dry out. The TLC-plates were eluted in AcN, EtAc, 1-propanol, H2O (85:20:50:40), whereafter the plates were heated 5 min at 167° C. to remove excess solvent. The plate was dipped up side down (i.e. by hold the plate on the edge near where the samples were applied) in 5% H2SO4:EtOH (95:5). The dipping solution was made daily. The plates were heated 3 min at 167° C. to visualize spots. Determination of spot intensity was done by scanning in a TLC scanner (CAMAG scanner 3, Muttenz, Switzerland) and quantification was done by drawing a standard-curve based on all maltose and isomaltose concentrations vs. spot intensities. Both maltose and isomaltose concentrations were calculated from this curve, using the fact that the spot intensity vs. concentration is equal for the two compounds. The isomaltose synthesis activity (IS activity) is calculated on basis of the isomaltose concentrations determined by TLC according to the following formula: As a measure of thermostability of the enzymes under the conditions used in the present experiments, the GAU activity was determined according to the above assay before and after incubation of enzymes in 15% glucose, 0.1M citrate buffer, pH 5.4 at 63° C. for 120 min. Data is presented as % activity lost. 400× Trace element solution: Dilute in 1000 ml of demi water: Anhudrous Citric Acid (175 g), FeSO4*7 H2O (200 g), ZnSO4*7 H2O (16 g), CuSO4*5 H2O (3.2 g), MnSO4*H2O (1.4 g), H3BO3 (0.8 g). It may be helpful to acidify this to get all components into solution. The solution was filtered and sterilized. LD-medium: Add to ˜800 ml of demi water: Casamino acids (9 g), MgSO4.7H2O (1 g), (NH4)2SO4 (5 g), KH2PO4 (4.5 g), CaCl2*2H2O (1 g), piperazine-1,4-bis(propanesulfonic acid (PIPPS) buffer (33 g), 400× 2×Amd S Base ager (1 litre): Mix KH2PO4 (30 g), 1M Acetamide (20 ml), 1M CsCl (20 ml), 20% MgSO4.7H2O (6 ml), 20% CaCl2.2H2O (6 ml), Initial Culture: Strains were grown on AmdS-Base agar plates. To produce agar plates minimal media agar was boiled and after cooling down to app. 50° C. it was diluted with 2× AmdS Base 1:1 and poured on petri dishes. After sporulation (app. 6-7 days) the plates were scraped with 2 ml saline 0.015% Tween 80. Approx 1 ml was added to glycerol tubes containing 500-600 μl 35% glycerol and stored at −80° C. The pre-culture fermentations were started directly from this spore suspension. Pre Culture: The medium is made by adding 2.5% glucose to the LD-medium, which is subsequently made up to 1 L. To produce biomass 50 μl spore suspension is added to 100 ml medium (sterilised in 500 ml shake flask). The flasks are incubated on a rotary shaker at 30° C., 180 rpm for 2 days, then 10 ml suspension is used to inoculate a new shake flask, which is incubated under similar conditions for 1 day. The content of this flask is used to inoculate a fermentor. Main Culture: To make 1 L of medium, 40 ml glucose/sophorose mix (Danisco, Jamsa, Finland) was added to the LD-medium and mede up to 1 L. 6 L fermentors containing 4 L of medium were inoculated with the pre-culture, and grown at pH 3.5 for approximately 16 hours at 34° C., until CER/OUR (Carbondioxide Excretion Rate/Oxygen Uptake Rate) started falling. Then temperature was lowered to 28° C., pH was raised to 4.0 and the fermentation was continued for approximately 80 hours. Brew Analysis with Determination of Real Degree of Fermentation (RDF) Analysis was carried out at using the following procedure: 70 g milled pilsner malt (Weyermann, Bamberg, Germany) was mashed with 266 ml water. The temperature cycle after mashing in (mixing malt and water) was: 140 minutes at 63.9° C., increasing to 73.9° C. over 10 minutes, 5 minutes at 73.9° C. At the end of mashing, the mashes were cooled, made up to 350 g and filtered. Filtrate volumes were measured after 30 minutes. The filtrated worts were sampled for specific gravity determination, then heated to 99° C. for 10 minutes in a water bath in order to destroy any residual glucoamylase activity. The heat treatment results in a loss of 1.5 g per 200 ml wort. The worts were fermented at 18° C. and 100 rpm in 500 ml conical flasks after yeast addition for at least 88 hours and no more than 120 hours. Specific gravity was determined on the ferments. A modified decoction mashing, using corn grist as adjunct was employed. The brewing protocol was modified from US 2009014247.40% of the malt was substituted with corn grist with a moisture content of 12.6% (Benntag Nordic; Nordgetreide GmBH Liibec, Germany). All corn grist was heated to 100° C. at 2° C./min, together with 54% of the water and 5% of the malt (well modified Pilsner malt; Fuglsang Denmark). 5 min rests were held at 72° C. and 80° C. and a 10 min rest was held at 100° C. Hereafter the adjunct was cooled to 64° C. and combined with the main mash, also at 64° C. Enzymes were added at this stage, and the 64° C. rest was extended to 250 min. After fermentation the RDF values were determined. Real degree of fermentation (RDF) value may be calculated according to the equation below: Where: RE=real extract=(0.1808×°Pinitial)+(0.8192×°Pfinal), °Pinitial is the specific gravity of the standardised worts before fermentation and °Pfinal is the specific gravity of the fermented worts expressed in degree plato. In the present context, Real degree of fermentation (RDF) was determined as follows: After fermentation samples were filtered and degassed. Specific gravity and alcohol concentration was determined on the ferments using a Beer Alcolyzer Plus and a DMA 5000 Density meter (both from Anton Paar, Graz, Austria). Based on these measurements, the real degree of fermentation (RDF) value is calculated, by the instrument, according to the equation below: Where: E(r) is the real extract in degree Plato (°P) and OE is the original extract in °P. Samples were diluted in citric acid (0.1 M)—di-sodium-hydrogen phosphate (0.2 M) buffer, pH 5.0, to obtain approx. OD590=0.7 in this assay. Three different dilutions of the sample were pre-incubated for 5 minutes at 40° C. At time=5 minutes, 1 Xylazyme tablet (crosslinked, dyed xylan substrate, Megazyme, Bray, Ireland) was added to the enzyme solution in a reaction volume of 1 ml. At time=15 minutes the reaction was terminated by adding 10 ml of 2% TRIS/NaOH, pH 12. Blanks were prepared using 1000 μl buffer instead of enzyme solution. The reaction mixture was centrifuged (1500×g, 10 minutes, 20° C.) and the OD of the supernatant was measured at 590 nm. One xylanase unit (XU) is defined as the xylanase activity increasing OD590 with 0.025 per minute. On incubation of Red-Pullulan (partially depolymerised pullulan, which is dyed with Procion Red MX-5B, from assay kit S-RPUL, Megazyme Int., Bray, Ireland) with pullulanase or limit-dextrinase the substrate is depolymerised by an endo-mechanism to produce low molecular-weight dyed fragments which remain in solution on addition of ethanol to the reaction mixture. High-molecular weight material is removed by centrifugation, and the colour of the supernatant is measured at 510 nm. Pullulanase in the assay solution is determined by reference to a standard curve. 0.5 g of powdered substrate was dissolved in to 25 mL of 0.5 M potassium chloride solution. Enzyme is diluted at least 10 times in buffer. If the resulting A510 reading was above 1.0 the enzyme was further diluted. In a test tube 1.0 mL of enzyme solution, pre-equilibrated to 40° C., was mixed with 0.5 mL substrate solution, pre-equilibrated to 40° C. The mix was incubated at 40° C. for 10 min. Reaction was terminated and high-molecular weight substrate was precipitated by the adding 2.5 mL ethanol (95% v/v). The tubes were equilibrate to room temperature for 10 min, then stirred for 10 sec on a vortex mixer and centrifuged at 1,000 g for 10 min. Supernatants were transferred to a 96 well plate and the absorbance of blank and reaction solutions was measured at 510 nm against distilled water. The blank reading was subtracted from the sample reading to obtain the A510 used in the formula below. Activity is determined from the formula: milli-PU/mL=360*A510+11. The blank is prepared by adding ethanol to the Red-Pullulan substrate before addition of the enzyme. One Unit of activity is defined as the amount of enzyme required to release one mole of D-glucose reducing sugar equivalents per minute from borohydride reduced pullulan, under the defined assay conditions (see Megazyme method S-RPUL 10/08, Megazyme Int., Bray, Ireland). Method is based on the release of reducing groups measured, by reference to a standard curve, as glucose from a 20 minute hydrolysis of 4% potato soluble starch at pH 4.5 and 50° C. One Soluble Starch Unit (SSU) is the activity which liberates 1 milligram of glucose equivalents per minute. 4% (w/v) potato soluble starch (Sigma, S 2630) solution in 0.05 M sodium acetate buffer, pH 4.5. The potato soluble starch is slurried in deionised water then added to vigorously boiling water in a flask. The starch solution is boiled, with stirring, for three minutes then cooled to 25° C. and acetic acid and sodium hydroxide solution added to give a 0.05 M sodium acetate buffer, pH 4.5, when made up to the final concentration. DNS Solution: 1 L of DNS solution is made up by adding to water: 16 g sodium hydroxide followed by 10 g 3-5 dinitro salicylic acid and then 300 g sodium potassium tartrate, each component being dissolved before the next is added. The solution is made up to volume and stored in the dark. Add 0.4 ml starch substrate and 0.1 ml 0.5M sodium acetate buffer, pH 4.5 to a test tube which is capped and equilibrated to temperature in a water bath set at 50° C. Add 0.1 ml of diluted enzyme solution and after 20 minutes stop the reaction by adding 0.1 ml 2% (w/v) NaOH. Run each enzyme assay in duplicate along with an enzyme blank. To each tube (assay and blank) add 1.5 ml water and 2.0 ml DNS solution, mix and place in a boiling water bath for 5 minutes then cool the tubes in an ice bath for 10 minutes. Let the tubes stand at room temperature for 20 minutes and read the absorbance at 543 nm. Construct a glucose standard curve corresponding to 0.0-1.0 mg glucose per 2.2 ml water, then adding 2.0 ml of DNS reagent and proceeding as described. Convert absorbance values (A543) of samples to mg of glucose using the standard curve, and calculate the ΔA543 mg glucose values [sample−blank] (ΔA543 must be between 0.2-0.4). Activity is determined from the formula: A To express the TrGA protein in SELs were constructed using the pDONR-TrGA entry vector ( 96 single colonies from each library were grown for 24 hrs at 37° C. in MTP containing 200 μL 2×YT medium with 100 μg/ml ampicillin. Cultures were used directly to amplify PCR fragments encompassing the region where a specific mutation was introduced. The specific PCR products obtained were sequenced using an ABI3100 sequence analyzer (Applied Biosystems). Each library contained from 15 to 19 different TrGA variants in the final expression vector. These variants were individually transformed into The SELs were transformed into For protoplast preparation, spores were grown for 16-24 hours at 24° C. in The transformation method was scaled down 10 fold. In general, transformation mixtures containing up to 600 ng of DNA and 1-5×105 protoplasts in a total volume of 25 μl were treated with 200 ml of 25% PEG solution, diluted with 2 volumes of 1.2 M sorbitol solution, mixed with 3% selective top agarose MM with acetamide (the same Minimal Medium as mentioned above but (NH4)2SO4 was substituted with 20 mM acetamide) and poured onto 2% selective agarose with acetamide either in 24 well microtiter plates or in a 20×20 cm Q-tray divided in 48 wells. The plates were incubated at 28° C. for 5 to 8 days. Spores from the total population of transformants regenerated on each individual well were harvested from the plates using a solution of 0.85% NaCl, 0.015% Tween 80. Spore suspensions were used to inoculate fermentations in 96 wells MTPs. In the case of 24 well MTPs, an additional plating step on a fresh 24 well MTP with selective acetamide MM was introduced in order to enrich the spore numbers. The transformants were fermented and the supernatants containing the expressed variant TrGA proteins were tested for various properties. In brief, 96-well filter plates (Corning Art. No. 3505) containing in each well 200 μl of LD-GSM medium (5.0 g/L (NH4)2SO4, 33 g/L 1,4-piperazinebis(propanesulfonic acid), pH 5.5, 9.0 g/L Casamino acids, 1.0 g/L KH2PO4, 1.0 g/L CaCl2.2H2O, 1.0 g/L MgSO4.7H2O, 2.5 ml/L of 1000× TrGA producing transformants were initially pre-grown in 250 ml shake flasks containing 30 ml of ProFlo medium. Proflo medium contained: 30 g/L α-lactose, 6.5 g/L (NH4)2SO4, 2 g/L KH2PO4, 0.3 g/L MgSO4.7H2O, 0.2 g/L CaCl2.2H2O, 1 ml/L 1000× trace element salt solution as mentioned above, 2 ml/L 10% Tween 80, 22.5 g/L ProFlo cottonseed flour (Traders protein, Memphis, Tenn.), 0.72 g/L CaCO3. After two days of growth at 28° C. and 140 rpm, 10% of the Proflo culture was transferred into a 250 ml shake flask containing 30 ml of Lactose Defined Medium. The composition of the Lactose Defined Medium was as follows: 5 g/L (NH4)2SO4, 33 g/L 1,4-piperazinebis (propanesulfonic acid) buffer, pH 5.5, 9 g/L casamino acids, 4.5 g/L KH2PO4, 1.0 g/L MgSO4.7H2O, 5 ml/L Mazu DF60-P antifoam (Mazur Chemicals, IL), 1 ml/L of 1000× trace element solution. 40 ml/L of 40% (w/v) lactose solution was added to the medium after sterilization. Shake flasks with the Lactose Defined Medium were incubated at 28° C., 140 rpm for 4-5 days. Mycelium was removed from the culture samples by centrifugation and the supernatant was analyzed for total protein content (BCA Protein Assay Kit, Pierce Cat. No. 23225) and GA activity, as described above in the Assays and Methods section. The protein profile of the whole broth samples was determined by SDS-PAGE electrophoresis. Samples of the culture supernatant were mixed with an equal volume of 2× sample loading buffer with reducing agent and separated on NUPAGE® Novex 10% Bis-Tris Gel with MES SDS Running Buffer (Invitrogen, Carlsbad, Calif., USA). Polypeptide bands were visualized in the SDS gel with SIMPLYBLUE SafeStain (Invitrogen, Carlsbad, Calif., USA). The thermal stability was measured according to above assay “Thermal stability assay 2”. The parent molecule under the conditions described had a residual activity of 87.2%, Table 3 shows the residual activity for the variants, which were selected from an initial screen for fermentation in large scale and further analysis. The material used was crude fermentation broth from shake flasks. Residual activity was calculated on basis of GAU activity before and after 120 min incubation at 63° C. in 0.1M citrate buffer pH 5.4, containing 15% glucose. Variants were tested according to above assays: “Starch hydrolysis activity” and “Determination of maltose and isomaltose synthesis by TLC”. The IS/SH ratio was calculated from the results of these analysis as described. Table 4 summarises the data for the variants selected for fermentation in large scale and further analysis. The material used was crude fermentation broth from shake flasks. All the variants shown in table 3 and 4 were grown in fermentors and GA enzyme was collected and purified (as described above under “Purification of TrGA variants”). The purified enzymes were reanalysed for IS/SH ratio as described above in Example 6 and thermostability was measured as described in Example 5. Brew analysis with determination of RDF value was carried out on the four variants which showed the best combination of IS/SH ratio and thermostability (Brew11, Brew1, Var16 and Var13) as described above under “Brew analysis with determinaiton of real degree of fermentation (RDF)”. RDF values are listed in Table 5. Based on data a selected set of variants with single substitutions were further characterized. These variants have single substitution at positions: 43, 44, 61, 73, 294, 417, 430, 431, 503, 511, 535, 539, and 563. Among these sites, 43, 44, and 294 were identified in a previous screening experiment in Additionally, combinatorial variants were constructed using the PCR method with substitutions among: 43, 44, 61, 73, 294, 417, 430, 431, 503, 511, 535, 539, and 563. Briefly, the combinatorial variants were constructed by using plasmid pDONR-TrGA ( CTCTCT [XbaI site] GAGAGGGG [GAP combinatorial variant][attB2 sites] CCCCAGAG[HindIII] AGAGAG This construct was treated with restriction enzymes Xba-I and HindIII. The digested fragments were ligated into Xba-I/HindIII treated pBC (a pUC19 derived vector). The ligation mixture was transformed to Variants were purified from large-scale fermentation, i.e., 100 ml or 500 ml fermentation, and PIs of thermal stability (Ts) and specific activities were determined. Specifically, specific activities were determined using different substrates, including DP2, DP3, DP4, DP5, DP6, DP7, cornstarch (CS), and liquefact (Liq). PIs are presented in Table 8. “N/D” in Table 8 stands for “not done.” The crystal structure of the TrGA identified in Example 11 in WO2009/067218 (Danisco US Inc., Genencor Division) page 89-93 incorporated herein by reference was superposed on the previously identified crystal structure of the Based on this analysis, sites were identified that could be mutated in TrGA and result in increased thermostability and/or specific activity. There sites include 108, 124, 175, and 316 at the active site. Also identified were specific pairwise variants Y47W/Y315F and Y47F/Y315W. Other sites identified were 143, D44, P45, D46, R122, R125, V181, E242, Y310, D313, V314, N317, R408, and N409. Because of the high structural homology, it is expected that beneficial variants found at sites in the TrGA would have similar consequence in The TrGA linker, residues 454-490 is defined as the segment spanning the region between two disulfide bridges, one between residues 222 and 453 and one between residues 491 and 587. Nine of the residues in the linker are prolines. From the crystal structure, the linker extends from the back of the molecule in a wide arc followed by an abrupt turn after the lysine 477 residue on the surface near the substrate binding surface. The linker extends as a random coil that is anchored by interactions of the side chains of Tyr 452, Pro 465, Phe 470, Gln 474, Pro 475, Lys 477, Val 480 and Tyr 486 to regions on the surface of the catalytic domain. The starch binding domain is composed of a beta-sandwich of two twisted beta sheets, tethered at one end by a disulfide bridge between Cys 491 and Cys 587 and at the other end, having a series of loops that comprise a binding site for starch connected by long loops. The structure of the TrGA SBD is quite similar to the averaged structure of the AnGA SBD determined by NMR (Sorimachi et al., Structure 5: 647-661 (1997)) and the SBD of beta amylase from Taken together, there appears to be a common pattern for the interactions between the linker and SBD with the catalytic domain. The interaction is in the form of an anchoring side chain that interacts with the surface area of the neighboring domain. In general, the anchor residue is found on the linker segment. In the case of interactions between the CD and SBD, the anchor residues can be contributed from either domain as in the case of residues Ile 43 and Phe 29 that come from the CD or residue 592, which comes from the SBD. The crystal structure of the TrGA complexed with the inhibitor acarbose has been determined. Crystals of the complex were obtained by soaking pre-grown native TrGA crystals in acarbose. After soaking for 3 days the crystals were mounted in a seal glass capillary tube and x-ray diffraction was collected with a Rigaku Raxis IV++ image plate detector to a resolution of 2.0 Å. The coordinates were fitted to a difference electron density map. The model was refined to an R-factor of 0.154 with an R-free of 0.201 for a total of 41276 reflection representing all data collected between 27 and 2.0 Å resolution. The model of the resulting refined structure is shown in Based on the knowledge that the presence of the SBD has an impact on hydrolysis of insoluble starch, it followed that there should be an interaction of the SBD with larger starch molecules. Thus, the structure of the TrGA was compared with known structures of (1) an acarbose bound CD of AaGA and (2) an SBD from Based on this model, sites were identified for which substitutions could be made in the TrGA SBD to result in increased stability and/or specific activity. Thus, two loops that are part of binding site 1 are likely candidates for alterations to increase or decrease binding to the larger starch molecule. These are loop 1 (aa 560-570) and loop 2 (aa 523-527). Because the two Trp (tryptophan) residues at amino acids 525 and 572 are likely involved directly in starch binding, they would not be as conducive to change. However, the underlying residues, including 516-518 would be conducive, as would the underlying residues 558-562. The loop from residues 570-578 is also a good candidate for alterations. Residues 534-541 are part of the binding site 2 that interacts with the catalytic site on the CD. Thus, these might be a good candidate for alterations that may increase or decrease specific activity. Because of the high structural homology of the TrGA SBD, it is expected that beneficial variants found at sites in Purified variant of the Table 9 below shows the RDF values obtained with different combinations of glucoamylase, pullulanase and alpha-amylase using the above described “Malt-adjunct brew analysis”-method. The glucoamylase, pullulanase and alpha-amylase activity were measured as described above. Three replicates were made for each dose. The average RDF and standard deviation are listed. For glucoamylases the amount of glucoamylase protein added/kg of grist is listed. Additionally the corresponding activity in GAU/kg of grist is listed. For alpha-amylase and pullulanase the number of enzyme units added/kg of grist is listed together with the corresponding amount of enzyme product (GC626 and DIAZYME® P10 respectively) added/kg of grist. *DIAZYME® X4 also contains some alpha-amylase activity. The number of units of alpha-amylase added when dosing this product is also listed in the table. It is seen from Table 9, dose 2 and 3 that BRW1 performs better in terms of RDF obtained than TrGA. This correlates well with the fact that the BRW1 variant has a lower level of reversion activity. When dosed at 1022 mg glucoamylase protein/kg of grist BRW1 performs on level with DIAZYME® X4 (compare dose 1 and 3). Note that the glucoamylase in DIAZYME® X4 ( When the dose of BRW1 is doubled from 1022 to 2044 mg/kg of grist, the RDF value increases from 83.2 to 84.8 (compare doses 3 and 4). RDF values can also be increased by adding auxiliary enzymes. When BRW1 is combined with alpha-amylase at 28172 SSU/kg of grist and pullulanase at 1961 PU/kg of grist the RDF value increases from 83.2 to 84.1 (compare doses 3 and 5). At high dose of BRW1 (2044 mg/kg of grist) there is also a benefit of adding auxiliary enzymes, but not as pronounced as with the low dose of BRW1 (compare differences in RDF between dose 3 and 5 and dose 4 and 6). Following are sequences, which are herein incorporated by reference in their entirety. The foregoing applications, and all documents cited therein or during their prosecution (“appin cited documents”) and all documents cited or referenced in the appin cited documents, and all documents cited or referenced herein (“herein cited documents”), and all documents cited or referenced in herein cited documents, together with any manufacturer's instructions, descriptions, product specifications, and product sheets for any products mentioned herein or in any document incorporated by reference herein, are hereby incorporated herein by reference, and may be employed in the practice of the invention. Various modifications and variations of the described methods and system of the disclosure will be apparent to those skilled in the art without departing from the scope and spirit of the disclosure. Although the disclosure has been described in connection with specific representative embodiments, it should be understood that the subject matters as claimed should not be unduly limited to such specific embodiments. Indeed, various modifications of the described modes for carrying out the disclosure that are obvious to those skilled in the art are intended to be within the scope of the following claims. The present invention relates to combinatorial variants of a parent glucoamylase that have altered properties for reducing the synthesis of condensation products during hydrolysis of starch. Accordingly the variants of a parent glucoamylase are suitable such as for use within brewing and glucose syrup production. Also disclosed are DNA constructs encoding the variants and methods of producing the glucoamylase variants in host cells. 1. A glucoamylase variant comprising the following amino acid substitutions:
a. 44R and 539R; or b. 44R, 61I and 539R, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase, wherein the glucoamylase variant has at least 80% sequence identity with SEQ ID NO: 1 or 2, or the parent glucoamylase, wherein the parent glucoamylase is SEQ ID NOs: 1, 2, 3, 5, 6, 7, 8, or 9. 2. The glucoamylase variant according to a. D44R and A539R; or b. D44R, N61I and A539R, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase, wherein the glucoamylase variant has at least 80% sequence identity with SEQ ID NO: 1 or 2, or the parent glucoamylase, wherein the parent glucoamylase is SEQ ID NOS: 1, 2, 3, 5, 6, 7, 8 or 9. 3-4. (canceled) 5. The glucoamylase variant according to 6-7. (canceled) 8. The glucoamylase variant of 9. (canceled) 10. The glucoamylase variant according to 11. The glucoamylase variant according to 12-17. (canceled) 18. The glucoamylase variant according to 19. (canceled) 20. The glucoamylase variant according to 21-25. (canceled) 26. A polynucleotide encoding a glucoamylase variant according to 27. A vector comprising the polynucleotide according to a. 44R and 539R; or b. 44R, 61I and 539R, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase, wherein the glucoamylase variant has at least 80% sequence identity with SEQ ID NO: 1 or 2, or the parent glucoamylase, wherein the parent glucoamylase is SEQ ID NOs: 1, 2, 3, 5, 6, 7, 8, or 9. 28-29. (canceled) 30. A cell capable of expressing a glucoamylase variant according to 31-33. (canceled) 34. A method of expressing a glucoamylase variant, the method comprising obtaining a cell according to 35-36. (canceled) 37. An enzymatic composition comprising at least one glucoamylase variant according to 38. (canceled) 39. The enzymatic composition according to 40-47. (canceled) 48. A method for producing a wort for brewing comprising forming a mash from a grist, and contacting the mash with a glucoamylase variant comprising the following amino acid substitutions:
a. 44R and 539R; or b. 44R, 61I and 539R, the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase, wherein the glucoamylase variant has at least 80% sequence identity with SEQ ID NO: 1 or 2 or the parent glucoamylase, wherein the parent glucoamylase is SEQ ID NOs: 1, 2, 3, 5, 6, 7, 8, or 9, or an enzymatic composition according to 49-59. (canceled)FIELD OF THE INVENTION
BACKGROUND OF THE INVENTION
SUMMARY OF THE INVENTION
BRIEF DESCRIPTION OF THE DRAWINGS
DETAILED DISCLOSURE OF THE INVENTION
1. Definitions and Abbreviations
1.1. Definitions
PU=1.2. Abbreviations
GAU glucoamylase unit
wt % weight percent
° C. degrees Centigrade
rpm revolutions per minute
H2O water
dH2O deionized water
dIH2O deionized water, Milli-Q filtration
aa or AA amino acid
bp base pair
kb kilobase pair
kD kilodaltons
g or gm grams
μg micrograms
mg milligrams
μl and μL microliters
ml and mL milliliters
mm millimeters
μmicrometer
M molar
mM millimolar
μM micromolar
U units
V volts
MW molecular weight
MWCO molecular weight cutoff
sec(s) or s(s) second/seconds
min(s) or m(s) minute/minutes
hr(s) or h(s) hour/hours
DO dissolved oxygen
ABS Absorbance
PSS physiological salt solution
m/v mass/volume
MTP microtiter plate
N Normal
DP2 disaccharides
DP>3 oligosaccharides, sugars having a degree of polymerization greater than 3
ppm parts per million
SBD starch binding domain
CD catalytic domain
PCR polymerase chain reaction
WT wild-type
2. Parent Glucoamylases
3. Glucoamylase Structural Homology
helix 1 residues 2-20, loop 1 residues 21-51, helix 2 residues 52-68, loop 2 residues 69-71, helix 3 residues 72-90, loop 3 residues 91-125, helix 4 residues 126-145, loop 4 residues 146, helix 5 residues 147-169, helix 6 residues 186-206, loop 6 residues 207-210, helix 7 residues 211-227, loop 7 residues 211-227, helix 8 residues 250-275, loop 8 residues 260-275, helix 9 residues 276-292, loop 9 residues 293-321, helix 10 residues 322-342, loop 10 residues 343-371, helix 11 residues 372-395, loop 11 residues 396-420, helix 12 residues 421-434, loop 12 residues 435-443, helix 13 residues 444-447, loop 13 residues 448-453 sheet 1′ residues 496-504, loop 1′ residues 505-511, sheet 2′ residues 512-517, interconnecting loop 2′ residues 518-543, sheet 3′ residues 544-552, loop 3′ residues 553, sheet 4′ residues 554-565, loop 4′ residues 566-567, sheet 5′ residues 568-572, inter-sheet segment residues 573-577, sheet 5a′ residues 578-582, loop 5′ residues 583-589, sheet 6′ residues 590-596, 4. Glucoamylase Variants
a) D44R and A539R; or
b) D44R, N61I and A539R,
a) D44R and A539R; or
b) D44R, N61I and A539R,
N61I/L417V/A431L/A539R;
I430/N61I/L417V/A431L/A539R;
N61I/L417V/A431L/A535R/A539R
I43Q/L417V/A431L/A535Ft/A539R;
I43Q/N61I/L417V/A431L/A535R/A539R;
I43Q/N61I/L417V/T430A/A431L/A535R/A539R;
I43Q/L417V/T430A/A431L/Q511H/A535R/A539R/N563I;
N61I/L417V/T430A/A431L/Q511H/A535R/A539R/N563I;
I43Q/N61I/L417V/T430A/A431L/Q511H/A535R/A539R/N563I;
I43R/N61I/L417V/T430A/A431L/A535R/A539R;
G73F/L417R/E503V/A539R/N563K;
I43R/G73F/L417R/E503V/A539R/N563K; and
I43R/G73F/E503V/Q511H/N563K.
L417V/A431L/A539R;
I430/L417V/A431L/A539R;
L417V/A431L/A535R/A539R
I43R/L417V/A431L/A539R;
L417R/A431L/A539R; or
L417G/A431L/A539R;
D44R/N61I/A539R;
D44R/A539R;
I430/D44C/L417V/E503A/Q511H/A539R;
I430/L417V/E503A/Q511H/A539R;
I430/D44C/N61I/L417V/E503A/Q511H/A539R;
I430/N61I/L417V/E503A/Q511H/A539R;
I43R/L417V/E503A/Q511H/A539R;
I43R/N61I/L417V/E503A/Q511H/A539R;
I43R/L417R/E503A/A539R;
I43R/N61I/L417R/E503A/Q511H/A539R;
G73F/T430A/Q511H;
I43R/G73F/T430A;
G73F/T430A/E503V/Q511H;
D44C/G73F/N563K;
D44C/G73F/E503V/Q511H;
D44C/G73F/N563K;
D44C/G73F/L417R/N563K;
D44C/G73F/N563K;
I43R/T43 GA;
I43Q/T430A;
I43Q/T430A/Q511H;
D44C/L417R/N563K;
L417V/T430A/A431L/Q511H/A53SR/A539R/N563I;
L417V/T430A/A431Q/Q511H/A535R/A539R/N563I;
L417V/T430A/Q511H/A535R/N563I;
L417V/T430A/Q511H/A539R/N563I;
G294C/L417R/A431L;
G294C/L417V/A431Q;
G294C/L417V/A431L/Q511H;
G294C/L417R/A431Q/Q511H;
L417R/A431L/Q511H;
L417V/A431Q/Q511H;
I43Q/T430A/Q511H/N61I;
I43Q/T430A/Q511H/L417V;
I43Q/T430A/Q511H/A431L;
I43Q/T430A/Q511H/E503A;
I43Q/T430A/Q511H/A539R;
I43Q/T430A/Q511H/N611/A539R;
I43Q/T430A/Q511H/L417V/A539R;
I43Q/T430A/Q511H/A431L/A539R;
I43Q/T430A/Q511H/A431L/E503A;
I43Q/T430A/Q511H/N61I/A539R/A431L;
I43Q/T430A/Q511H/L417V/A539R/A431L;
I43Q/Q511H/N61I;
I43Q/Q511H/L417V;
I43Q/Q511H/A431L;
I43Q/Q511H/A539R;
I43Q/Q511H/A539R/N61I;
I43Q/Q511H/A539R/E503A;
I43Q/Q511H/A539R/T430M;
I43Q/Q511H/A539R/T430M/N61I;
I43Q/Q511H/A539R/T430M/N61I/L417V;
I43R/T430A/E503V/A535R/N563K;
D44R/E503A/Q511H/N563I;
E503A/N563I;
I43R/T430A/E503A/Q511H/N563K;
D44R/T430A/Q511H/A535R;
L417V/A431L/A539R;
L417V/A431L/A539R/I43Q;
L417V/A431L/A539R/N61I;
L417V/A431L/A539R/A535R;
L417V/A431L/A539R/I43Q/N61I;
L417V/A431L/A539R/N61I/A535R;
L417V/A431L/A539R/A535R/I43Q;
L417V/A431L/A539R/I43Q/N61I/A535R;
L417V/A431L/A539R/I43Q/N61I/A535R/T430A;
L417V/T430A/A431L/Q511H/A535R/A539R/N563I/I43Q;
L417V/T430A/A431L/Q511H/A535R/A539R/N563I/N61I;
L417V/T430A/A431L/Q511H/A535R/A539R/N563I/I43Q/N61I;
L417V/A431L/A539R/I43R;
L417V/A431L/A539R/143R/N61I;
L417V/A431L/A539R/I43R/N61I/A535R/T430A;
L417R/A431L/A539R;
L417G/A431L/A539R;
G73F/E503V/N563K/L417R/A539R;
G73F/E503V/N563K/I43R/L417R/A539R; and
G73F/E503V/N563K/I43R/Q511H
D44R/N61I/A539R;
D44R/A539R;
I43Q/D44C/L417V/E503A/Q511H/A539R;
I43Q/L417V/E503A/Q511H/A539R;
I43Q/D44C/N61I/L417V/E503A/Q511H/A539R;
I43Q/N61I/L417V/E503A/Q511H/A539R;
I43R/L417V/E503A/Q511H/A539R;
I43R/N61I/L417V/E503A/Q511H/A539R;
I43R/L417R/E503A/A539R;
I43R/N61I/L417R/E503A/Q511H/A539R;
L417V/T430A/A431L/Q511H/A535R/A539R/N563I;
L417V/T430A/A431Q/Q511H/A535R/A539R/N563I;
L417V/T430A/Q511H/A539R/N563I;
I43Q/T430A/Q511H/A539R;
I43Q/T430A/Q511H/N61I/A539R;
I43Q/T430A/Q511H/L417V/A539R;
I43Q/T430A/Q511H/A431L/A539R;
I43Q/0JT430A/Q511H/N61I/A539R/A431L;
I43Q/0T430A/Q511H/L417V/A539R/A431L;
I43Q/Q511H/A539R;
I43Q/Q511H/A539R/N61I;
I43Q/Q511H/A539R/E503A;
I43Q/Q511H/A539R/T430M;
I43Q/Q511H/A539R/T430M/N61I;
I43Q/Q511H/A539R/T430M/N61I/L417V;
L417V/A431L/A539R;
L417V/A431L/A539R/I43Q;
L417V/A431L/A539R/N61I;
L417V/A431L/A539R/A535R;
L417V/A431L/A539R/I43Q/N61I;
L417V/A431L/A539R/N61I/A535R;
L417V/A431L/A539R/A535R/I43Q;
L417V/A431L/A539R/I43Q/N61I/A535R;
L417V/A431L/A539R/I43Q/N61I/A535R/T430A;
L417V/T430A/A431L/Q511H/A535R/A539R/N563I/I43Q;
L417V/T430A/A431L/Q511H/A535R/A539R/N563I/N61I;
L417V/T430A/A431L/Q511H/A535R/A539R/N563I/I43Q/N61I;
L417V/A431L/A539R/I43R;
L417V/A431L/A539R/I43R/N61I;
L417V/A431L/A539R/I43R/N61I/A535R/T430A;
L417R/A431L/A539R;
L417G/A431L/A539R;
G73F/E503V/N563K/I43R/L417R/A539R
D44R/N61I/A539R;
D44R/A539R;
I43Q/D44C/L417V/E503A/Q511H/A539R;
I43Q/L417V/E503A/Q511H/A539R;
I43Q/D44C/N61I/L417V/E503A/Q511H/A539R;
I43Q/N61I/L417V/E503A/Q511H/A539R;
I43R/L417V/E503A/Q511H/A539R;
I43R/N61I/L417V/E503A/Q511H/A539R;
I43R/L417R/E503A/A539R;
I43R/N61I/L417R/E503A/Q511H/A539R;
L417V/T430A/A431L/Q511H/A535R/A539R/N563I;
L417V/T430A/A431Q/Q511H/A535R/A539R/N563I;
L417V/T430A/Q511H/A539R/N563I;
I43Q/T430A/Q511H/A539R;
I43Q/T430A/Q511H/N61I/A539R;
I43Q/T430A/Q511H/L417V/A539R;
I43Q/T430A/Q511H/A431L/A539R;
I43Q/T430A/Q511H/N61I/A539R/A431L;
I43Q/T430A/Q511H/L417V/A539R/A431L;
I43Q/Q511H/A539R;
I43Q/Q511H/A539R/N61I;
I43Q/Q511H/A539R/E503A;
I43Q/Q511H/A539R/T430M;
I43Q/Q511H/A539R/T430M/N61I;
I43Q/Q511H/A539R/T430M/N61I/L417V;
L417V/A431L/A539R;
L417V/A431L/A539R/I43Q;
L417V/A431L/A539R/N61I;
L417V/A431L/A539R/A535R;
L417V/A431L/A539R/I43Q/N61I;
L417V/A431L/A539R/N61I/A535R;
L417V/A431L/A539R/A535R/I43Q;
L417V/A431L/A539R/I43Q/N61I/A535R;
L417V/A431L/A539R/I43Q/N61I/A535R/T430A;
L417V/T430A/A431L/Q511H/A535R/A539R/N563I/I43Q;
L417V/T430A/A431L/Q511H/A535R/A539R/N563I/N61I;
L417V/T430A/A431L/Q511H/A535R/A539R/N563I/I43Q/N61I;
L417V/A431L/A539R/I43R;
L417V/A431L/A539R/I43R/N61I;
L417V/A431L/A539R/143R/N61I/A535R/T430A;
L417R/A431L/A539R;
L417G/A431L/A539R;
G73F/E503V/N563K/L417R/A539R; and
G73F/E503V/N563K/I43R/L417R/A539R
D44R/N61I/A539R;
D44R/A539R;
L417V/A431L/A539R;
L417V/A431L/A539R/I43Q;
L417V/A431L/A539R/N61I;
D44R/N61I/A539R;
D44R/A539R;
Sequence homology between various fungal glucoamylases AaGA AnGA AoGA HgGA HvGA TrGA AaGA 100 95 58 53 57 56 AnGA 100 59 53 57 56 AoGA 100 55 56 56 HgGA 100 61 63 HvGA 100 91 TrGA 100 5. Characterization of Variant Glucoamylases
5.1. Variant Glucoamylases with Altered Thermostability
5.2. Variant Glucoamylases with Altered Specific Activity
5.3. Variant Glucoamylases with Both Altered Thermostability and Altered Specific Activity
5.4. Variant Glucoamylases with Production of Fermentable Sugar(s)
5.5 Variant Glucoamylases with a Altered Ratio Between Isomaltose Synthesis and Starch Hydrolysis Activity (IS/SH Ratio)
6. Polynucleotides Encoding Glucoamylases
7. Production of Glucoamylases
7.1. DNA Constructs and Vectors
7.2. Host Cells and Transformation of Host Cells
7.3. Production of Glucoamylases
8. Compositions and Uses
Embodiment 1
Embodiment 2
Embodiment 3
Embodiment 4
Embodiment 5
Embodiment 6
Embodiment 7
Embodiment 8
Embodiment 9
Embodiment 10
Embodiment 11
Embodiment 12
Embodiment 13
Embodiment 14
Embodiment 15
Embodiment 16
Embodiment 17
Embodiment 18
Embodiment 19
Embodiment 20
Embodiment 21
Embodiment 22
Embodiment 23
Embodiment 24
Embodiment 25
Embodiment 26
Embodiment 27
Embodiment 28
Embodiment 29
Embodiment 30
Embodiment 31
Embodiment 32
Embodiment 33
Embodiment 34
Embodiment 35
Embodiment 36
Embodiment 37
Embodiment 38
Embodiment 39
Embodiment 40
Embodiment 41
Embodiment 42
Embodiment 43
Embodiment 44
Embodiment 45
Embodiment 46
Embodiment 47
Embodiment 48
Embodiment 49
Embodiment 50
Embodiment 51
Embodiment 52
Embodiment 53
Embodiment 54
Embodiment 55
Embodiment 56
Embodiment 57
Embodiment 58
Embodiment 59
Embodiment 60
the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase.
Embodiment 61
the positions corresponding to the respective position in SEQ ID NO:2.
Embodiment 62
Embodiment 63
Embodiment 64
Embodiment 65
Embodiment 66
Embodiment 67
Embodiment 68
Embodiment 69
Embodiment 70
Embodiment 71
Embodiment 72
Embodiment 73
Embodiment 74
Embodiment 75
Embodiment 76
Embodiment 77
Embodiment 78
Embodiment 79
Embodiment 80
Embodiment 81
Embodiment 82
Embodiment 83
Embodiment 84
Embodiment 85
Embodiment 86
Embodiment 87
Embodiment 88
Embodiment 89
Embodiment 90
Embodiment 91
Embodiment 92
Embodiment 93
Embodiment 94
Embodiment 95
Embodiment 96
Embodiment 97
Embodiment 98
Embodiment 99
Embodiment 100
The method according to embodiment 96-99, wherein the additional enzyme is amylase and pullulanase.
Embodiment 101
Embodiment 102
Embodiment 103
Embodiment 104
Embodiment 105
Embodiment 106
Embodiment 107
Embodiment 108
Embodiment 109
Embodiment 110
Embodiment 111
Embodiment 112
Embodiment 113
wherein a glucoamylase variant according to any one of embodiments 50-77 is added to: step (a) and/or step (b) and/or step (c).
Embodiment 114
Embodiment 115
Embodiment 116
Embodiment 117
Embodiment 118
Embodiment 119
Embodiment 120
Embodiment 121
Embodiment 122
Further Embodiment 1
the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase, wherein the glucoamylase variant has at least 80% sequence identity with SEQ ID NO: 1 or 2, or the parent glucoamylase.
Further Embodiment 2
the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase, wherein the glucoamylase variant has at least 80% sequence identity with SEQ ID NO: 1 or 2, or the parent glucoamylase.
Further Embodiment 3
the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase, wherein the glucoamylase variant has at least 80% sequence identity with SEQ ID NO: 1 or 2, or the parent glucoamylase.
Further Embodiment 4
the positions corresponding to the respective position in SEQ ID NO:2 or an equivalent position in a parent glucoamylase, wherein the glucoamylase variant has at least 80% sequence identity with SEQ ID NO: 1 or 2, or the parent glucoamylase.
Further Embodiment 5
Further Embodiment 6
Further Embodiment 7
Further Embodiment 8
Further Embodiment 9
Further Embodiment 10
Further Embodiment 11
Further Embodiment 12
Further Embodiment 13
Further Embodiment 14
Further Embodiment 15
Further Embodiment 16
Further Embodiment 17
Further Embodiment 18
Further Embodiment 19
Further Embodiment 20
Further Embodiment 21
Further Embodiment 22
Further Embodiment 23
Further Embodiment 24
Further Embodiment 25
Further Embodiment 26
Further Embodiment 27
Further Embodiment 28
Further Embodiment 29
Further Embodiment 30
Further Embodiment 31
Further Embodiment 32
Further Embodiment 33
Further Embodiment 34
Further Embodiment 35
Further Embodiment 36
Further Embodiment 37
Further Embodiment 38
Further Embodiment 39
Further Embodiment 40
Further Embodiment 41
Further Embodiment 42
Further Embodiment 43
Further Embodiment 44
Further Embodiment 45
Further Embodiment 46
Further Embodiment 47
Further Embodiment 48
Further Embodiment 49
Further Embodiment 50
Further Embodiment 51
Further Embodiment 52
Further Embodiment 53
Further Embodiment 54
Further Embodiment 55
Further Embodiment 56
wherein a glucoamylase variant according to any one of further embodiments 1-25 or an enzymatic composition according to any one of further embodiments 36-48 is added to: step (a) and/or step (b) and/or step (c).
Further Embodiment 57
Further Embodiment 58
Further Embodiment 59
Further Embodiment 60
EXAMPLES
Assays and Methods
Thermal Stability Assay 1
Hexokinase Activity Assay
Data Analysis and Calculation of Performance Index of Ethanol Screening Assay
Purification of TrGA Variants
Protein Quantification of Purified TrGA Variants
Liquefact Assay
Evaluation of Performance of TrGA Variant in Ethanol Fermentations
Ethanol and Carbohydrate Determinations
Determination of GAU Activity
Starch Hydrolysis Activity (SH Activity):
Isomaltose Hydrolysis Activity
Determination of Glucose Concentration
Determination of Maltose and Isomaltose Synthesis by TLC
Thermal Stability Assay 2
Production of GA by Fermentation
Pure Malt Brew Analysis
Malt-Adjunct Brew Analysis
Xylanase Assay Method
Pullulanase Assay Method
Principle:
Substrate:
Buffer: Sodium Acetate, 200 mM, pH 5.0
Enzyme Preparation:
Assay Procedure:
Alpha-Amylase Assay (SSU) Method
Principle:
Substrate:
Assay Procedure:
Color Development:
Standard Curve:
Calculation Of Enzyme Activity (SSU)
SSU/ml or Example 1
Construction of TrGA Site Evaluation Libraries (SELs) in the pTTT Vector for Expression in
Primers used to generate TrGA SELs AA- F/ position R DNA Sequence 5′ to 3′ pDONR201- F TCGCGTTAACGCTAGCATGGATCTC (SEQ ID NO: 13) pDONR201- R TCGCGTTAACGCTAGCATGGATCTC (SEQ ID NO: 14) 4 F CGTCACCAAGAGGTCTGTTGACNNSTTCATCAGCAC CGAGACGCC (SEQ ID NO: 15) 4 R GTCAACAGACCTCTTGGTGACGTCG (SEQ ID NO: 16) 5 F CACCAAGAGGTCTGTTGACGACNNSATCAGCACCG AGACGCCTATTGC (SEQ ID NO: 17) 5 R GTCGTCAACAGACCTCTTGGTGAC (SEQ ID NO: 18) 10 F TGACGACTTCATCAGCACCGAGNNSCCTATTGCA CTG (SEQ ID NO: 19) 10 R CTCGGTGCTGATGAAGTCGTC (SEQ ID NO: 20) 12 F TCATCAGCACCGAGACGCCTNNSGCACTGAACAATC TTCTTTGCA (SEQ ID NO: 21) 12 R AGGCGTCTCGGTGCTGATGAAGTCG (SEQ ID NO: 22) 14 F CAGCACCGAGACGCCTATTGCANNSAACAATCTT CTT (SEQ ID NO: 23) 14 R TGCAATAGGCGTCTCGGTGCT (SEQ ID NO: 24) 15 F CACCGAGACGCCTATTGCACTGNNSAATCTTCTT TGC (SEQ ID NO: 25) 15 R CAGTGCAATAGGCGTCTCGGT (SEQ ID NO: 26) 23 F CAATCTTCTTTGCAATGTTGGTNNSGATGGATGC CGT (SEQ ID NO: 27) 23 R ACCAACATTGCAAAGAAGATTG (SEQ ID NO: 28) 24 F TTCTTTGCAATGTTGGTCCTNNSGGATGCCGTGCATT CGGCACAT (SEQ ID NO: 29) 24 R AGGACCAACATTGCAAAGAAGATTG (SEQ ID NO: 30) 29 F GTCCTGATGGATGCCGTGCANNSGGCACATCAGCTGG TGCGGTGA (SEQ ID NO: 31) 29 R TGCACGGCATCCATCAGGACCAACA (SEQ ID NO: 32) 42 F TGCGGTGATTGCATCTCCCAGCNNSATTGACCC GGAC (SEQ ID NO: 33) 42 R GCTGGGAGATGCAATCACCGCA (SEQ ID NO: 34) 43 F TGATTGCATCTCCCAGCACANNSGACCCGGACTACTA TTACATGT (SEQ ID NO: 35) 43 R TGTGCTGGGAGATGCAATCACCGCA (SEQ ID NO: 36) 44 F TTGCATCTCCCAGCACAATTNNSCCGGACTACTATTA CATGTGGA (SEQ ID NO: 37) 44 R AATTGTGCTGGGAGATGCAATCACC (SEQ ID NO: 38) 45 F CATCTCCCAGCACAATTGACNNSGACTACTATTACA TGTGGACGC (SEQ ID NO: 39) 45 R GTCAATTGTGCTGGGAGATGCAATC (SEQ ID NO: 40) 46 F CTCCCAGCACAATTGACCCGNNSTACTATTACATGT GGACGCGAGA (SEQ ID NO: 41) 46 R CGGGTCAATTGTGCTGGGAGATGCA (SEQ ID NO: 42) 47 F CCAGCACAATTGACCCGGACNNSTATTACATGTGGA CGCGAGATA (SEQ ID NO: 43) 47 R GTCCGGGTCAATTGTGCTGGGAGAT (SEQ ID NO: 44) 49 F CAATTGACCCGGACTACTATNNSATGTGGACGCGAG ATAGCGCTC (SEQ ID NO: 45) 49 R ATAGTAGTCCGGGTCAATTGTGCTG (SEQ ID NO: 46) 51 F ACCCGGACTACTATTACATGNNSACGCGAGATAGC GCTCTTGTCT (SEQ ID NO: 47) 51 R CATGTAATAGTAGTCCGGGTCAATT (SEQ ID NO: 48) 59 F GACGCGAGATAGCGCTCTTGTCNNSAAGAACCTC ATC (SEQ ID NO: 49) 59 R GACAAGAGCGCTATCTCGCGT (SEQ ID NO: 50) 60 F GCGAGATAGCGCTCTTGTCTTCNNSAACCTCATC GAC (SEQ ID NO: 51) 60 R GAAGACAAGAGCGCTATCTCG (SEQ ID NO: 52) 61 F AGATAGCGCTCTTGTCTTCAAGNNSCTCATCGAC CGC (SEQ ID NO: 53) 61 R CTTGAAGACAAGAGCGCTATC (SEQ ID NO: 54) 65 F TGTCTTCAAGAACCTCATCGACNNSTTCACCGAA ACG (SEQ ID NO: 55) 65 R GTCGATGAGGTTCTTGAAGAC (SEQ ID NO: 56) 67 F CAAGAACCTCATCGACCGCTTCNNSGAAACGTA CGAT (SEQ ID NO: 57) 67 R GAAGCGGTCGATGAGGTTCTT (SEQ ID NO: 58) 68 F GAACCTCATCGACCGCTTCACCNNSACGTACGA TGCG (SEQ ID NO: 59) 68 R GGTGAAGCGGTCGATGAGGTT (SEQ ID NO: 60) 70 F TCGACCGCTTCACCGAAACGNNSGATGCGGGCCT GCAGCGCCGCA (SEQ ID NO: 61) 70 R CGTTTCGGTGAAGCGGTCGATGAGG (SEQ ID NO: 62) 72 F CCGCTTCACCGAAACGTACGATNNSGGCCTGCA GCGC (SEQ ID NO: 63) 72 R ATCGTACGTTTCGGTGAAGCGG (SEQ ID NO: 64) 73 F CTTCACCGAAACGTACGATGCGNNSCTGCAGCG CCGC (SEQ ID NO: 65) 73 R CGCATCGTACGTTTCGGTGAA (SEQ ID NO: 66) 75 F AAACGTACGATGCGGGCCTGNNSCGCCGCATCGAG CAGTACATTA (SEQ ID NO: 67) 75 R CAGGCCCGCATCGTACGTTTCGGTG (SEQ ID NO: 68) 76 F CGTACGATGCGGGCCTGCAGNNSCGCATCGAGCAGT ACATTACTG (SEQ ID NO: 69) 76 R CTGCAGGCCCGCATCGTACGTTTCG (SEQ ID NO: 70) 94 F CTCTCCAGGGCCTCTCTAACNNSTCGGGCTCCCTCGC GGACGGCT (SEQ ID NO: 71) 94 R GTTAGAGAGGCCCTGGAGAGTGACC (SEQ ID NO: 72) 97 F GGGCCTCTCTAACCCCTCGGGCNNSCTCGCGGAC GGC (SEQ ID NO: 73) 97 R GCCCGAGGGGTTAGAGAGGCC (SEQ ID NO: 74) 98 F CCTCTCTAACCCCTCGGGCTCCNNSGCGGACGG CTCT (SEQ ID NO: 75) 98 R GGAGCCCGAGGGGTTAGAGAG (SEQ ID NO: 76) 99 F CTCTAACCCCTCGGGCTCCCTCNNSGACGGCTCT GGT (SEQ ID NO: 77) 99 R GAGGGAGCCCGAGGGGTTAGA (SEQ ID NO: 78) 100 F ACCCCTCGGGCTCCCTCGCGNNSGGCTCTGGTCTC GGCGAGCCCA (SEQ ID NO: 79) 100 R CGCGAGGGAGCCCGAGGGGTTAGAG (SEQ ID NO: 80) 102 F CTCGGGCTCCCTCGCGGACGGCNNSGGTCTCGGC GAG (SEQ ID NO: 81) 102 R GCCGTCCGCGAGGGAGCCCGA (SEQ ID NO: 82) 110 F TGGTCTCGGCGAGCCCAAGTTTNNSTTGACCCTG AAG (SEQ ID NO: 83) 110 R AAACTTGGGCTCGCCGAGACCA (SEQ ID NO: 84) 111 F TCTCGGCGAGCCCAAGTTTGAGNNSACCCTGAA GCCT (SEQ ID NO: 85) 111 R CTCAAACTTGGGCTCGCCGAG (SEQ ID NO: 86) 113 F CGAGCCCAAGTTTGAGTTGACCNNSAAGCCTTTC ACC (SEQ ID NO: 87) 113 R GGTCAACTCAAACTTGGGCTC (SEQ ID NO: 88) 114 F CCAAGTTTGAGTTGACCCTGNNSCCTTTCACCGGC AACTGGGGTC (SEQ ID NO: 89) 114 R CAGGGTCAACTCAAACTTGGGCTCG (SEQ ID NO: 90) 116 F TTGAGTTGACCCTGAAGCCTNNSACCGGCAACTGG GGTCGACCGCA (SEQ ID NO: 91) 116 R AGGCTTCAGGGTCAACTCAAACTTG (SEQ ID NO: 92) 119 F CCCTGAAGCCTTTCACCGGCNNSTGGGGTCGACCG CAGCGGGATG (SEQ ID NO: 93) 119 R GCCGGTGAAAGGCTTCAGGGTCAAC (SEQ ID NO: 94) 122 F CTTTCACCGGCAACTGGGGTNNSCCGCAGCGGGAT GGCCCAGCTC (SEQ ID NO: 95) 122 R ACCCCAGTTGCCGGTGAAAGGCTTC (SEQ ID NO: 96) 125 F GCAACTGGGGTCGACCGCAGNNSGATGGCCCAGCT CTGCGAGCCA (SEQ ID NO: 97) 125 R CTGCGGTCGACCCCAGTTGCCGGTG (SEQ ID NO: 98) 133 F GGATGGCCCAGCTCTGCGAGCCNNSGCCTTGATT GGA (SEQ ID NO: 99) 133 R GGCTCGCAGAGCTGGGCCATCC (SEQ ID NO: 100) 137 F TGCGAGCCATTGCCTTGATTNNSTACTCAAAGTGGC TCATCAACA (SEQ ID NO: 101) 137 R AATCAAGGCAATGGCTCGCAGAGCT (SEQ ID NO: 102) 140 F CATTGCCTTGATTGGATACTCANNSTGGCTCAT CAAC (SEQ ID NO: 103) 140 R TGAGTATCCAATCAAGGCAATG (SEQ ID NO: 104) 144 F TGGATACTCAAAGTGGCTCATCNNSAACAACTAT CAG (SEQ ID NO: 105) 144 R GATGAGCCACTTTGAGTATCC (SEQ ID NO: 106) 145 F ATACTCAAAGTGGCTCATCAACNNSAACTATCAG TCG (SEQ ID NO: 107) 145 R GTTGATGAGCCACTTTGAGTA (SEQ ID NO: 108) 146 F CAAAGTGGCTCATCAACAACNNSTATCAGTCGACT GTGTCCAACG (SEQ ID NO: 109) 146 R GTTGTTGATGAGCCACTTTGAGTAT (SEQ ID NO: 110) 147 F AAAGTGGCTCATCAACAACAACNNSCAGTCGACT GTG (SEQ ID NO: 111) 147 R GTTGTTGTTGATGAGCCACTT (SEQ ID NO: 112) 148 F GGCTCATCAACAACAACTATNNSTCGACTGTGTCCA ACGTCATCT (SEQ ID NO: 113) 148 R ATAGTTGTTGTTGATGAGCCACTTT (SEQ ID NO: 114) 152 F CAACAACTATCAGTCGACTGTGNNSAACGTCATC TGG (SEQ ID NO: 115) 152 R CACAGTCGACTGATAGTTGTT (SEQ ID NO: 116) 153 F CAACTATCAGTCGACTGTGTCCNNSGTCATCTGG CCT (SEQ ID NO: 117) 153 R GGACACAGTCGACTGATAGTT (SEQ ID NO: 118) 164 F GCCTATTGTGCGCAACGACCTCNNSTATGTTGCC CAGT (SEQ ID NO: 119) 164 R GAGGTCGTTGCGCACAATAGG (SEQ ID NO: 120) 169 F ACCTCAACTATGTTGCCCAGNNSTGGAACCAAACC GGCTTTGACC (SEQ ID NO: 121) 169 R CTGGGCAACATAGTTGAGGTCGTTG (SEQ ID NO: 122) 172 F ATGTTGCCCAGTACTGGAACNNSACCGGCTTTGACC TCTGGGAAG (SEQ ID NO: 123) 172 R GTTCCAGTACTGGGCAACATAGTTG (SEQ ID NO: 124) 175 F AGTACTGGAACCAAACCGGCNNSGACCTCTGGGAA GAAGTCAATG (SEQ ID NO: 125) 175 R GCCGGTTTGGTTCCAGTACTGGGCA (SEQ ID NO: 126) 178 F ACCAAACCGGCTTTGACCTCNNSGAAGAAGTCAATG GGAGCTCAT (SEQ ID NO: 127) 178 R GAGGTCAAAGCCGGTTTGGTTCCAG (SEQ ID NO: 128) 180 F CCGGCTTTGACCTCTGGGAANNSGTCAATGGGAGCT CATTCTTTA (SEQ ID NO: 129) 180 R TTCCCAGAGGTCAAAGCCGGTTTGG (SEQ ID NO: 130) 181 F GCTTTGACCTCTGGGAAGAANNSAATGGGAGCTCAT TCTTTACTG (SEQ ID NO: 131) 181 R TTCTTCCCAGAGGTCAAAGCCGGTT (SEQ ID NO: 132) 182 F CTTTGACCTCTGGGAAGAAGTCNNSGGGAGCTCATT C (SEQ ID NO: 133) 182 R GACTTCTTCCCAGAGGTCAAAG (SEQ ID NO: 134) 204 F TGTCGAGGGCGCCACTCTTGCTNNSACTCTTGGCCA G (SEQ ID NO: 135) 204 R AGCAAGAGTGGCGCCCTCGAC (SEQ ID NO: 136) 205 F CGAGGGCGCCACTCTTGCTGCCNNSCTTGGCCAGTC G (SEQ ID NO: 137) 205 R GGCAGCAAGAGTGGCGCCCTC (SEQ ID NO: 138) 208 F CTCTTGCTGCCACTCTTGGCNNSTCGGGAAGCGCTTA TTCATCTG (SEQ ID NO: 139) 208 R GCCAAGAGTGGCAGCAAGAGTGGCG (SEQ ID NO: 140) 211 F CCACTCTTGGCCAGTCGGGANNSGCTTATTCATCTGT TGCTCCCC (SEQ ID NO: 141) 211 R TCCCGACTGGCCAAGAGTGGCAGCA (SEQ ID NO: 142) 214 F TGGCCAGTCGGGAAGCGCTTATNNSTCTGTTGCTCC C (SEQ ID NO: 143) 214 R ATAAGCGCTTCCCGACTGGCC (SEQ ID NO: 144) 216 F GTCGGGAAGCGCTTATTCATCTNNSGCTCCCCAGGT T (SEQ ID NO: 145) 216 R AGATGAATAAGCGCTTCCCGA (SEQ ID NO: 146) 219 F CGCTTATTCATCTGTTGCTCCCNNSGTTTTGTGCTT T (SEQ ID NO: 147) 219 R GGGAGCAACAGATGAATAAGC (SEQ ID NO: 148) 228 F TGTGCTTTCTCCAACGATTCNNSGTGTCGTCTGGTG GATACGTCG (SEQ ID NO: 149) 228 R GAATCGTTGGAGAAAGCACAAAAC CT (SEQ ID NO: 150) 229 F GTGCTTTCTCCAACGATTCTGGNNSTCGTCTGGTG GA (SEQ ID NO: 151) 229 R CCAGAATCGTTGGAGAAAGCA (SEQ ID NO: 152) 230 F CTTTCTCCAACGATTCTGGGTGNNSTCTGGTGGAT ACG (SEQ ID NO: 153) 230 R CACCCAGAATCGTTGGAGAAA (SEQ ID NO: 154) 231 F TCTCCAACGATTCTGGGTGTCGNNSGGTGGATAC GTC (SEQ ID NO: 155) 231 R CGACACCCAGAATCGTTGGAGA (SEQ ID NO: 156) 236 F GGTGTCGTCTGGTGGATACGTCNNSTCCAACATC AACAC (SEQ ID NO: 157) 236 R GACGTATCCACCAGACGACAC (SEQ ID NO: 158) 239 F TGGTGGATACGTCGACTCCAACNNSAACACCAAC GAG (SEQ ID NO: 159) 239 R GTTGGAGTCGACGTATCCACC (SEQ ID NO: 160) 240 F TGGATACGTCGACTCCAACATCNNSACCAACGAG GGCA (SEQ ID NO: 161) 240 R GATGTTGGAGTCGACGTATCCA (SEQ ID NO: 162) 241 F ATACGTCGACTCCAACATCAACNNSAACGAGGGCAG GAC (SEQ ID NO: 163) 241 R GTTGATGTTGGAGTCGACGTA (SEQ ID NO: 164) 242 F TCGACTCCAACATCAACACCNNSGAGGGCAGGACTG GCAAGGATG (SEQ ID NO: 165) 242 R GGTGTTGATGTTGGAGTCGACGTAT (SEQ ID NO: 166) 243 F ACTCCAACATCAACACCAACNNSGGCAGGACTGGCA AGGATGTCA (SEQ ID NO: 167) 243 R GTTGGTGTTGATGTTGGAGTCGACG (SEQ ID NO: 168) 244 F CTCCAACATCAACACCAACGAGNNSAGGACTGGCA AG (SEQ ID NO: 169) 244 R CTCGTTGGTGTTGATGTTGGAGT (SEQ ID NO: 170) 245 F ACATCAACACCAACGAGGGCNNSACTGGCAAGGAT GTCAACTCCG (SEQ ID NO: 171) 245 R GCCCTCGTTGGTGTTGATGTTGGAGT (SEQ ID NO: 172) 263 F TTCCATCCACACCTTCGATCCCNNSCTTGGCTGTG AC (SEQ ID NO: 173) 263 R GGGATCGAAGGTGTGGATGGA (SEQ ID NO: 174) 264 F CATCCACACCTTCGATCCCAACNNSGGCTGTGACG CA (SEQ ID NO: 175) 264 R GTTGGGATCGAAGGTGTGGAT (SEQ ID NO: 176) 265 F CCACACCTTCGATCCCAACCTTNNSTGTGACGCAG GC (SEQ ID NO: 177) 265 R AAGGTTGGGATCGAAGGTGTG (SEQ ID NO: 178) 268 F CGATCCCAACCTTGGCTGTGACNNSGGCACCTTCC AGC (SEQ ID NO: 179) 268 R GTCACAGCCAAGGTTGGGATC (SEQ ID NO: 180) 269 F TCCCAACCTTGGCTGTGACGCANNSACCTTCCAG CCA (SEQ ID NO: 181) 269 R TGCGTCACAGCCAAGGTTGGG (SEQ ID NO: 182) 276 F AGGCACCTTCCAGCCATGCAGTNNSAAAGCGCTC TCC (SEQ ID NO: 183) 276 R ACTGCATGGCTGGAAGGTGCC (SEQ ID NO: 184) 284 F CAAAGCGCTCTCCAACCTCAAGNNSGTTGTCGAC TCCT (SEQ ID NO: 185) 284 R CTTGAGGTTGGAGAGCGCTTT (SEQ ID NO: 186) 291 F GGTTGTTGTCGACTCCTTCCGCNNSATCTACGGC GTG (SEQ ID NO: 187) 291 R GCGGAAGGAGTCGACAACAAC (SEQ ID NO: 188) 292 F TTGTCGACTCCTTCCGCTCCNNSTACGGCGTGAAC AAGGGCATTC (SEQ ID NO: 189) 292 R GGAGCGGAAGGAGTCGACAACAACC (SEQ ID NO: 190) 294 F ACTCCTTCCGCTCCATCTACNNSGTGAACAAGGGCA TTCCTGCCG (SEQ ID NO: 191) 294 R GTAGATGGAGCGGAAGGAGTCGACA (SEQ ID NO: 192) 297 F GCTCCATCTACGGCGTGAACNNSGGCATTCCTGCCGG TGCTGCCG (SEQ ID NO: 193) 297 R GTTCACGCCGTAGATGGAGCGGAAG (SEQ ID NO: 194) 300 F CTACGGCGTGAACAAGGGCATTNNSGCCGGTGCTGC CG (SEQ ID NO: 195) 300 R AATGCCCTTGTTCACGCCGTA (SEQ ID NO: 196) 301 F CGGCGTGAACAAGGGCATTCCTNNSGGTGCTGCCG TC (SEQ ID NO: 197) 301 R AGGAATGCCCTTGTTCACGCC (SEQ ID NO: 198) 303 F GAACAAGGGCATTCCTGCCGGTNNSGCCGTCGCCA TT (SEQ ID NO: 199) 303 R ACCGGCAGGAATGCCCTTGTT (SEQ ID NO: 200) 309 F GTGCTGCCGTCGCCATTGGCNNSTATGCAGAGGAT GTGTACTACA (SEQ ID NO: 201) 309 R GCCAATGGCGACGGCAGCACCGGCA (SEQ ID NO: 202) 310 F CTGCCGTCGCCATTGGCCGGNNSGCAGAGGATGTGT ACTACAACG (SEQ ID NO: 203) 310 R CCGGCCAATGGCGACGGCAGCACCG (SEQ ID NO: 204) 311 F TGCCGTCGCCATTGGCCGGTATNNSGAGGATGTG TAC (SEQ ID NO: 205) 311 R ATACCGGCCAATGGCGACGGC (SEQ ID NO: 206) 313 F CCATTGGCCGGTATGCAGAGNNSGTGTACTACAA CGGCAACCCTT (SEQ ID NO: 207) 313 F CCATTGGCCGGTATGCAGAGNNSGTGTACTACAAC GGCAACCCTT (SEQ ID NO: 208) 313 R CTCTGCATACCGGCCAATGGCGACG (SEQ ID NO: 209) 313 R CTCTGCATACCGGCCAATGGCGACG (SEQ ID NO: 210) 314 F TTGGCCGGTATGCAGAGGATNNSTACTACAACGGCAA CCCTTGGT (SEQ ID NO: 211) 314 R ATCCTCTGCATACCGGCCAATGGCG (SEQ ID NO: 212) 315 F GCCGGTATGCAGAGGATGTGNNSTACAACGGCAACC CTTGGTATC (SEQ ID NO: 213) 315 R CACATCCTCTGCATACCGGCCAATG (SEQ ID NO: 214) 316 F GGTATGCAGAGGATGTGTACNNSAACGGCAACCCTT GGTATCTTG (SEQ ID NO: 215) 316 R GTACACATCCTCTGCATACCGGCCAAT (SEQ ID NO: 216) 317 F ATGCAGAGGATGTGTACTACNNSGGCAACCCTTGGTA TCTTGCTA (SEQ ID NO: 217) 317 F ATGCAGAGGATGTGTACTACNNSGGCAACCCTTGGTA TCTTGCTA (SEQ ID NO: 218) 317 R GTAGTACACATCCTCTGCATACCGGC (SEQ ID NO: 219) 317 R GTAGTACACATCCTCTGCATACCGGC (SEQ ID NO: 220) 321 F TGTACTACAACGGCAACCCTNNSTATCTTGCTACATT TGCTGCTG (SEQ ID NO: 221) 321 F TGTACTACAACGGCAACCCTNNSTATCTTGCTACATT TGCTGCTG (SEQ ID NO: 222) 321 R AGGGTTGCCGTTGTAGTACACATCC (SEQ ID NO: 223) 321 R AGGGTTGCCGTTGTAGTACACATCC (SEQ ID NO: 224) 338 F GCAGCTGTACGATGCCATCTACNNSTGGAAGAAGA CG (SEQ ID NO: 225) 338 R GTAGATGGCATCGTACAGCTG (SEQ ID NO: 226) 340 F ACGATGCCATCTACGTCTGGNNSAAGACGGGCTCC ATCACGGTGA (SEQ ID NO: 227) 340 R CCAGACGTAGATGGCATCGTACAGC (SEQ ID NO: 228) 341 F ATGCCATCTACGTCTGGAAGNNSACGGGCTCCATCA CGGTGACCG (SEQ ID NO: 229) 341 R CTTCCAGACGTAGATGGCATCGTAC AGC (SEQ ID NO: 230) 342 F ATGCCATCTACGTCTGGAAGAAGNNSGGCTCCA TCACG (SEQ ID NO: 231) 342 R CTTCTTCCAGACGTAGATGGC (SEQ ID NO: 232) 344 F CTACGTCTGGAAGAAGACGGGCNNSATCACGG TGACC (SEQ ID NO: 233) 344 R GCCCGTCTTCTTCCAGACGTAG (SEQ ID NO: 234) 346 F CTGGAAGAAGACGGGCTCCATCNNSGTGACCGCC ACCTC (SEQ ID NO: 235) 346 R GATGGAGCCCGTCTTCTTCCA (SEQ ID NO: 236) 349 F GACGGGCTCCATCACGGTGACCNNSACCTCCCTG GCC (SEQ ID NO: 237) 349 R GGTCACCGTGATGGAGCCCGT (SEQ ID NO: 238) 350 F GCTCCATCACGGTGACCGCCNNSTCCCTGGCCTTC TTCCAGGAGC (SEQ ID NO: 239) 350 R GGCGGTCACCGTGATGGAGCCCGTC (SEQ ID NO: 240) 356 F CCACCTCCCTGGCCTTCTTCNNSGAGCTTGTTCCTGG CGTGACGG (SEQ ID NO: 241) 356 R GAAGAAGGCCAGGGAGGTGGCGGTC (SEQ ID NO: 242) 359 F CCTGGCCTTCTTCCAGGAGCTTNNSCCTGGCGTGA CG (SEQ ID NO: 243) 359 R AAGCTCCTGGAAGAAGGCCAG (SEQ ID NO: 244) 361 F CTTCTTCCAGGAGCTTGTTCCTNNSGTGACGGCC GGG (SEQ ID NO: 245) 361 R AGGAACAAGCTCCTGGAAGAA (SEQ ID NO: 246) 363 F AGGAGCTTGTTCCTGGCGTGNNSGCCGGGACCTA CTCCAGCAGCT (SEQ ID NO: 247) 363 R CACGCCAGGAACAAGCTCCTGGAAG (SEQ ID NO: 248) 364 F GGAGCTTGTTCCTGGCGTGACGNNSGGGACCTACT CC (SEQ ID NO: 249) 364 R CGTCACGCCAGGAACAAGCTC (SEQ ID NO: 250) 368 F GCGTGACGGCCGGGACCTACNNSAGCAGCTCTTCG ACCTTTACCA (SEQ ID NO: 251) 368 R GTAGGTCCCGGCCGTCACGCCAGGA (SEQ ID NO: 252) 369 F TGACGGCCGGGACCTACTCCNNSAGCTCTTCGACC TTTACCAACA (SEQ ID NO: 253) 369 R GGAGTAGGTCCCGGCCGTCACGCCA (SEQ ID NO: 254) 375 F CTCCAGCAGCTCTTCGACCTTTNNSAACATCATC AACG (SEQ ID NO: 255) 375 R AAAGGTCGAAGAGCTGCTGGA (SEQ ID NO: 256) 376 F GCAGCTCTTCGACCTTTACCNNSATCATCAACGCC GTCTCGACAT (SEQ ID NO: 257) 376 R GGTAAAGGTCGAAGAGCTGCTGGAG (SEQ ID NO: 258) 379 F TTCGACCTTTACCAACATCATCNNSGCCGTCTCG ACA (SEQ ID NO: 259) 379 R GATGATGTTGGTAAAGGTCGA (SEQ ID NO: 260) 382 F TACCAACATCATCAACGCCGTCNNSACATACGC CGAT (SEQ ID NO: 261) 382 R GACGGCGTTGATGATGTTGGT (SEQ ID NO: 262) 390 F GACATACGCCGATGGCTTCCTCNNSGAGGCTGCC AAG (SEQ ID NO: 263) 390 R GAGGAAGCCATCGGCGTATGT (SEQ ID NO: 264) 391 F ATACGCCGATGGCTTCCTCAGCNNSGCTGCCAAG TAC (SEQ ID NO: 265) 391 R GCTGAGGAAGCCATCGGCGTA (SEQ ID NO: 266) 393 F CGATGGCTTCCTCAGCGAGGCTNNSAAGTACGTC CCC (SEQ ID NO: 267) 393 R AGCCTCGCTGAGGAAGCCATC (SEQ ID NO: 268) 394 F TGGCTTCCTCAGCGAGGCTGCCNNSTACGTCCCC GCC (SEQ ID NO: 269) 394 R GGCAGCCTCGCTGAGGAAGCC (SEQ ID NO: 270) 395 F TCCTCAGCGAGGCTGCCAAGNNSGTCCCCGCCGACG GTTCGCTGG (SEQ ID NO: 271) 395 R CTTGGCAGCCTCGCTGAGGAAGCCA (SEQ ID NO: 272) 398 F AGGCTGCCAAGTACGTCCCCNNSGACGGTTCGCTGGC CGAGCAGTT (SEQ ID NO: 273) 398 R GGGGACGTACTTGGCAGCCTCGCTG (SEQ ID NO: 274) 401 F AGTACGTCCCCGCCGACGGTNNSCTGGCCGAGCAG TTTGACCGCA (SEQ ID NO: 275) 401 R ACCGTCGGCGGGGACGTACTTGGCAG (SEQ ID NO: 276) 408 F CGCTGGCCGAGCAGTTTGACNNSAACAGCGGCACTCC GCTGTCTG (SEQ ID NO: 277) 408 R GTCAAACTGCTCGGCCAGCGAACCG (SEQ ID NO: 278) 409 F TGGCCGAGCAGTTTGACCGCNNSAGCGGCACTCCGCT GTCTGCGC (SEQ ID NO: 279) 409 R GCGGTCAAACTGCTCGGCCAGCGAA (SEQ ID NO: 280) 410 F GGCCGAGCAGTTTGACCGCAACNNSGGCACTCCG CTG (SEQ ID NO: 281) 410 R GTTGCGGTCAAACTGCTCGGC (SEQ ID NO: 282) 412 F AGTTTGACCGCAACAGCGGCNNSCCGCTGTCTGCGC TTCACCTGA (SEQ ID NO: 283) 412 R GCCGCTGTTGCGGTCAAACTGCTCG (SEQ ID NO: 284) 415 F GCAACAGCGGCACTCCGCTGNNSGCGCTTCACCTGA CGTGGTCGT (SEQ ID NO: 285) 415 R CAGCGGAGTGCCGCTGTTGCGGTCA (SEQ ID NO: 286) 417 F CAGCGGCACTCCGCTGTCTGCGNNSCACCTGACGT GGT (SEQ ID NO: 287) 417 R CGCAGACAGCGGAGTGCCGCT (SEQ ID NO: 288) 418 F GCACTCCGCTGTCTGCGCTTNNSCTGACGTGGTCGT ACGCCTCGT (SEQ ID NO: 289) 418 R AAGCGCAGACAGCGGAGTGCCGCTG (SEQ ID NO: 290) 421 F TGTCTGCGCTTCACCTGACGNNSTCGTACGCCTCGTT CTTGACAG (SEQ ID NO: 291) 421 R CGTCAGGTGAAGCGCAGACAGCGGA (SEQ ID NO: 292) 430 F GTACGCCTCGTTCTTGACAGCCNNSGCCCGTCGG GCT (SEQ ID NO: 293) 430 R GGCTGTCAAGAACGAGGCGTA (SEQ ID NO: 294) 431 F CGCCTCGTTCTTGACAGCCACGNNSCGTCGGGC TGGC (SEQ ID NO: 295) 431 R CGTGGCTGTCAAGAACGAGGC (SEQ ID NO: 296) 433 F TCTTGACAGCCACGGCCCGTNNSGCTGGCATCGTG CCCCCCTCGT (SEQ ID NO: 297) 433 R ACGGGCCGTGGCTGTCAAGAACGAG (SEQ ID NO: 298) 436 F CCACGGCCCGTCGGGCTGGCNNSGTGCCCCCCTCGT GGGCCAACA (SEQ ID NO: 299) 436 R GCCAGCCCGACGGGCCGTGGCTGTC (SEQ ID NO: 300) 442 F TGGCATCGTGCCCCCCTCGTGGNNSAACAGCAG CGCT (SEQ ID NO: 301) 442 R CCACGAGGGGGGCACGATGCC (SEQ ID NO: 302) 443 F CATCGTGCCCCCCTCGTGGGCCNNSAGCAGCGCT AGC (SEQ ID NO: 303) 443 R GGCCCACGAGGGGGGCACGAT (SEQ ID NO: 304) 444 F CGTGCCCCCCTCGTGGGCCAACNNSAGCGCTAGC ACG (SEQ ID NO: 305) 444 R GTTGGCCCACGAGGGGGGCAC (SEQ ID NO: 306) 448 F GTGGGCCAACAGCAGCGCTAGCNNSATCCCCT CGACG (SEQ ID NO: 307) 451 F GCAGCGCTAGCACGATCCCCNNSACGTGCTC CGGCGCGTCCGTGG (SEQ ID NO: 308) 451 R GGGGATCGTGCTAGCGCTGCTGTTG (SEQ ID NO: 309) 493 F CTACACGCCCCTGCCCTGCGCGNNSCCAACCTCC GTG (SEQ ID NO: 310) 493 R CGCGCAGGGCAGGGGCGTGTA (SEQ ID NO: 311) 494 F CACGCCCCTGCCCTGCGCGACCNNSACCTCCGTG GCC (SEQ ID NO: 312) 494 R GGTCGCGCAGGGCAGGGGCGT (SEQ ID NO: 313) 495 F GCCCCTGCCCTGCGCGACCCCANNSTCCGTGGCC GTC (SEQ ID NO: 314) 495 R TGGGGTCGCGCAGGGCAGGGG (SEQ ID NO: 315) 501 F CCCAACCTCCGTGGCCGTCACCNNSCACGAGCTC GTGT (SEQ ID NO: 316) 501 R GGTGACGGCCACGGAGGTTGG (SEQ ID NO: 317) 502 F AACCTCCGTGGCCGTCACCTTCNNSGAGCTCGTG TCG (SEQ ID NO: 318) 502 R GAAGGTGACGGCCACGGAGGT (SEQ ID NO: 319) 503 F CTCCGTGGCCGTCACCTTCCACNNSCTCGTGTCGA CACA (SEQ ID NO: 320) 503 R GTGGAAGGTGACGGCCACGGA (SEQ ID NO: 321) 508 F CTTCCACGAGCTCGTGTCGACANNSTTTGGCCAG ACG (SEQ ID NO: 322) 508 R TGTCGACACGAGCTCGTGGAA (SEQ ID NO: 323) 511 F GCTCGTGTCGACACAGTTTGGCNNSACGGTCAAGGTG (SEQ ID NO: 324) 511 R GCCAAACTGTGTCGACACGAG (SEQ ID NO: 325) 514 F CACAGTTTGGCCAGACGGTCNNSGTGGCGGGCAACG CCGCGGCCC (SEQ ID NO: 326) 514 R GACCGTCTGGCCAAACTGTGTCGAC (SEQ ID NO: 327) 517 F TGGCCAGACGGTCAAGGTGGCGNNSAACGCCGCGGC CCTGGG (SEQ ID NO: 328) 517 R CGCCACCTTGACCGTCTGGCCAAACTG (SEQ ID NO: 329) 518 F CCAGACGGTCAAGGTGGCGGGCNNSGCCGCGGCCCT GGGCAACT (SEQ ID NO: 330) 518 R GCCCGCCACCTTGACCGTCTGGCCAAA (SEQ ID NO: 331) 519 F GACGGTCAAGGTGGCGGGCAACNNSGCGGCCCTGGG CAACT (SEQ ID NO: 332) 519 R GTTGCCCGCCACCTTGACCGTCTGGCC (SEQ ID NO: 333) 520 F GGTCAAGGTGGCGGGCAACGCCNNSGCCCTGGGCAA CTGGA (SEQ ID NO: 334) 520 R GGCGTTGCCCGCCACCTTGACCGTCTG (SEQ ID NO: 335) 525 F CAACGCCGCGGCCCTGGGCAACNNSAGCACGAGCGCC GCCG (SEQ ID NO: 336) 525 R GTTGCCCAGGGCCGCGGCGTTGCCCGC (SEQ ID NO: 337) 527 F CGCGGCCCTGGGCAACTGGAGCNNSAGCGCCGCCGT GGCTC (SEQ ID NO: 338) 527 R GCTCCAGTTGCCCAGGGCCGCGGCGTT (SEQ ID NO: 339) 531 F CAACTGGAGCACGAGCGCCGCCNNSGCTCTGGACGC CGTCA (SEQ ID NO: 340) 531 R GGCGGCGCTCGTGCTCCAGTTGCCCAG (SEQ ID NO: 341) 533 F GAGCACGAGCGCCGCCGTGGCTNNSGACGCCGTCAAC TATGC (SEQ ID NO: 342) 533 R AGCCACGGCGGCGCTCGTGCTCCAGTT (SEQ ID NO: 343) 535 F GAGCGCCGCCGTGGCTCTGGACNNSGTCAACTATGCC GATA (SEQ ID NO: 344) 535 R GTCCAGAGCCACGGCGGCGCTCGTGCT (SEQ ID NO: 345) 536 F CGCCGCCGTGGCTCTGGACGCCNNSAACTATGCCGAT AACC (SEQ ID NO: 346) 536 R GGCGTCCAGAGCCACGGCGGCGCTCGT (SEQ ID NO: 347) 537 F CGCCGTGGCTCTGGACGCCGTCNNSTATGCCGAT AAC (SEQ ID NO: 348) 537 F CGCCGTGGCTCTGGACGCCGTCNNSTATGCCGATAAC CACCCC (SEQ ID NO: 349) 537 R GACGGCGTCCAGAGCCACGGCGGCGCT (SEQ ID NO: 350) 537 R GACGGCGTCCAGAGCCACGGCGGCGCT (SEQ ID NO: 351) 538 F CGTGGCTCTGGACGCCGTCAACNNSGCCGATAACCAC CCCC (SEQ ID NO: 352) 538 R GTTGACGGCGTCCAGAGCCACGGCGGCG (SEQ ID NO: 353) 539 F GGCTCTGGACGCCGTCAACTATNNSGATAACCACCCC CTGT (SEQ ID NO: 354) 539 R ATAGTTGACGGCGTCCAGAGCCACGGC (SEQ ID NO: 355) 540 F TCTGGACGCCGTCAACTATGCCNNSAACCACCCCCTG TGGATT (SEQ ID NO: 356) 540 R GGCATAGTTGACGGCGTCCAGAGCCAC (SEQ ID NO: 357) 541 F GGACGCCGTCAACTATGCCGATNNSCACCCCCTGTGGA TTGGG (SEQ ID NO: 358) 541 R ATCGGCATAGTTGACGGCGTCCAGAGC (SEQ ID NO: 359) 545 F CTATGCCGATAACCACCCCCTGNNSATTGGGACGGTC AACCTC (SEQ ID NO: 360) 545 R CAGGGGGTGGTTATCGGCATAGTTGAC (SEQ ID NO: 361) 546 F TGCCGATAACCACCCCCTGTGGNNSGGGACGGTCAA CCTCGAG (SEQ ID NO: 362) 546 R CCACAGGGGGTGGTTATCGGCATAGTT (SEQ ID NO: 363) 547 F CGATAACCACCCCCTGTGGATTNNSACGGTCAACCTC GAGGCT (SEQ ID NO: 364) 547 R AATCCACAGGGGGTGGTTATCGGCATA (SEQ ID NO: 365) 549 F CCACCCCCTGTGGATTGGGACGNNSAACCTCGAGGC TGGAGAC (SEQ ID NO: 366) 549 R CGTCCCAATCCACAGGGGGTGGTTATC (SEQ ID NO: 367) 551 F CCTGTGGATTGGGACGGTCAACNNSGAGGCTGGAGA CGTCGTG (SEQ ID NO: 368) 551 R GTTGACCGTCCCAATCCACAGGGGGTG (SEQ ID NO: 369) 561 F TGGAGACGTCGTGGAGTACAAGNNSATCAATGTGGG CCAAGAT (SEQ ID NO: 370) 561 R CTTGTACTCCACGACGTCTCCAGCCTC (SEQ ID NO: 371) 563 F CGTCGTGGAGTACAAGTACATCNNSGTGGGCCAAG ATGGCTCC (SEQ ID NO: 372) 563 R GATGTACTTGTACTCCACGACGTCTCC (SEQ ID NO: 373) 567 F CAAGTACATCAATGTGGGCCAANNSGGCTCCGTGAC CTGGGAG (SEQ ID NO: 374) 567 R TTGGCCCACATTGATGTACTTGTACTC (SEQ ID NO: 375) 569 F CATCAATGTGGGCCAAGATGGCNNSGTGACCTGGGA GAGTGAT (SEQ ID NO: 376) 569 R GCCATCTTGGCCCACATTGATGTACTTG (SEQ ID NO: 377) 577 F CGTGACCTGGGAGAGTGATCCCNNSCACACTTACAC GGTTCCT (SEQ ID NO: 378) 577 R GGGATCACTCTCCCAGGTCACGGAGCC (SEQ ID NO: 379) 579 F CTGGGAGAGTGATCCCAACCACNNSTACACGGTTCC TGCGGTG (SEQ ID NO: 380) 579 R GTGGTTGGGATCACTCTCCCAGGTCAC (SEQ ID NO: 381) 583 F TCCCAACCACACTTACACGGTTNNSGCGGTGGCTTG TGTGACG (SEQ ID NO: 382) 583 R AACCGTGTAAGTGTGGTTGGGATCACT (SEQ ID NO: 383) Example 2
Transformation of TrGA SELs into
Example 3
Fermentation of
Example 4
Preparation of the Whole Broth Samples from GA-Producing Transformants
Example 5
Thermal stability of the variants
Thermostability for selected TrGA variants, shown as residual activity after incubation for 120 min at 63° C. in 0.1M citrate buffer pH 5.4, containing 15% glucose. Variant Residual activity D44R/N61I/A539R (BRW 84.2 11) L417R/A431L/A539R 88.5 (VAR16) D44R/A539R (BRW 1) 99.0 N61I/L417V/A431L/A539R (VAR3) 86.2 I43R/L417V/A431L/A539R 89.8 (VAR13) BRW 2 92.4 I43Q/D44C/N61I/L417V/ 86.6 E503A/Q511H/A539R (ALL3) I43Q/D44C/L417V/E503A/ 90.1 Q511H (ALL1) I43R/N61I/L417R/E503A/ 84.6 Q511H/A539R (ALL8) I43Q/N61I/T430M/Q511H/ 83.0 A539R (RB19) I43Q/N61I/T430A/A431L/ 82.3 Q511H/A539R (RB10) Diazyme X4 (AnGA reference 72.3 product) Diazyme TR8 (TrGA reference 87.2 product) I43R/G73F/T430A (C2 88.3 Negative Control) I43Q/L417V/Q511H (RB13 74.1 Negative Control) Example 6
Determination of Isomaltose Synthesis and Starch Hydrolysis and Ratio Thereof
Isomaltose synthesis activity (IS), starch hydrolysis activity (SH) and IS/SH ratio of selected TrGA variants Variant Iso- Iso- (Parent maltose Starch maltose glucaoamylase synthesis hydro- synthesis TrGA, SEQ ID M/min lysis Relative to (IS/SH) No: 2) *10E−05 M/min DiazymeX4 *10E−04 D44R/N61I/A539R 2.7 0.078 1.1 3.4 (BRW 11) L417R/A431L/A539R 3.4 0.078 1.4 4.4 (VAR16) D44R/A539R (BRW 1) 3.2 0.071 1.4 4.5 N61I/L417V/A431L/ 4.3 0.089 1.5 4.8 A539R (VAR3) I43R/L417V/A431L/ 4.1 0.082 1.6 5.0 A539R (VAR13) BRW 2 3.9 0.079 1.6 5.0 I43Q/D44C/N61I/ 3.8 0.074 1.6 5.1 L417V/E503A/Q511H/ A539R (ALL3) I43Q/D44C/L417V/ 3.7 0.072 1.6 5.2 E503A/Q511H (ALL1) I43R/N61I/L417R/ 4.3 0.079 1.7 5.4 E503A/Q511H/A539R (ALL8) I43Q/N61I/T430M/ 4.7 0.085 1.8 5.6 Q511H/A539R (RB19) I43Q/N61I/T430A/ 5.3 0.089 1.8 5.9 A431L/Q511H/A539R (RB10) Diazyme X4 (AnGA 1.0 3.2 reference product) Diazyme TR8 (TrGA 2.5 7.9 reference product) I43R/G73F/T430A (C2 8.7 0.0789 5.0 16 Negative Control) I43Q/L417V/Q511H 8.1 0.0508 3.4 11 (RB13 Negative Control) Example 7
Brew Analysis with Determination of Real Degree of Fermentation (RDF)
RDF values of selected purified TrGA-variants, purified wild type TrGA and purified AnGA. Below values were obtained using the above described “Pure malt brew analysis”-method. Purified GA RDF STDEV AnGA (purified from DIAZYME ® 82.5 0.064 X4) TrGA (purified from DIAZYME ® 82.0 0.028 TR8) D44R/N61I/A539R (BRW 11) 82.50 0.005 D44R/A539R (BRW 1) 82.33 0.050 L417R/A431L/A539R (VAR16) 81.93 0.113 I43R/L417V/A431L/A539R 81.86 0.085 (VAR13) Example 8
Construction and Characterization of Combinatorial Variants
PIs of a selected set of single site variants, each of which is obtained from a 500 ml fermentation. P.I. P.I. P.I. P.I. DP7- CornStarch- Thermal Liquefact- Variants FPLC FPLC Stability FPLC N61I 1.16 1.35 1.00 1.66 A431L 1.15 1.38 1.18 1.51 L417V 1.18 1.32 1.02 1.40 A431Q 1.06 1.20 0.92 1.24 G294C 1.01 0.84 0.94 1.23 N563K 1.07 1.12 1.97 1.15 Q511H 1.05 1.09 1.52 1.13 T430M 1.05 1.15 0.89 1.09 E503A 1.08 1.16 1.40 1.09 I43Q 1.11 1.24 0.94 1.08 A539R 1.15 1.37 1.43 1.08 I43R 1.03 1.07 1.41 1.07 L417R 1.23 1.27 1.51 1.04 T430A 1.13 1.35 1.23 1.04 G73F 1.06 1.06 1.45 1.03 D44R 0.97 1.06 1.46 0.98 N563I 1.09 1.22 2.06 0.92 D44C 0.80 0.82 0.96 0.91 E503V 1.17 1.07 1.66 0.88 A535R 1.09 1.44 1.47 0.85 Primers used to construct combinatorial variants SEQ ID Primer DNA sequence NO: Var1 Basic-1 GAGAGAGTGCGGGCCTCTTCGCTATTTCTAGA 391 Var1 Basic-2 CAAAATAAAATCATTATTTGTCTAGAAATAGCGAAGAGGC 392 Var1 Basic-3 CAAATAATGATTTTATTTTGACTGATAGTGACCTGTTCGT 393 Var1 Basic-4 TTGCTCATCAATGTGTTGCAACGAACAGGTCACTATCAGT 394 Var1 Basic-5 TGCAACACATTGATGAGCAATGCTTTTTTATAATGCCAAC 395 Var1 Basic-6 AGCCTGCTTTTTTGTACAAAGTTGGCATTATAAAAAAGCA 396 Var1 Basic-7 TTTGTACAAAAAAGCAGGCTATGCACGTCCTGTCGACTGC 397 Var1 Basic-8 CAACGGAGCCGAGCAGCACCGCAGTCGACAGGACGTGCAT 398 Var1 Basic-9 GGTGCTGCTCGGCTCCGTTGCCGTTCAAAAGGTCCTGGGA 399 Var1 Basic-10 AGACCGCTTGATCCTGGTCTTCCCAGGACCTTTTGAACGG 400 Var1 Basic-11 AGACCAGGATCAAGCGGTCTGTCCGACGTCACCAAGAGGT 401 Var1 Basic-12 GCTGATGAAGTCGTCAACAGACCTCTTGGTGACGTCGGAC 402 Var1 Basic-13 CTGTTGACGACTTCATCAGCACCGAGACGCCTATTGCACT 403 Var1 Basic-14 CATTGCAAAGAAGATTGTTCAGTGCAATAGGCGTCTCGGT 404 Var1 Basic-15 GAACAATCTTCTTTGCAATGTTGGTCCTGATGGATGCCGT 405 Var1 Basic-16 CCAGCTGATGTGCCGAATGCACGGCATCCATCAGGACCAA 406 Var1 Basic-17 GCATTCGGCACATCAGCTGGTGCGGTGATTGCATCTCCCA 407 Var1 Basic-18 GTAGTCCGGGTCAATTGTGCTGGGAGATGCAATCACCGCA 408 Var1 Basic-19 GCACAATTGACCCGGACTACTATTACATGTGGACGCGAGA 409 Var1 Basic-20 TCTTGAAGACAAGAGCGCTATCTCGCGTCCACATGTAATA 410 Var1 Basic-21 TAGCGCTCTTGTCTTCAAGAACCTCATCGACCGCTTCACC 411 Var1 Basic-22 AGGCCCGCATCGTACGTTTCGGTGAAGCGGTCGATGAGGT 412 Var1 Basic-23 GAAACGTACGATGCGGGCCTGCAGCGCCGCATCGAGCAGT 413 Var1 Basic-24 AGTGACCTGGGCAGTAATGTACTGCTCGATGCGGCGCTGC 414 Var1 Basic-25 ACATTACTGCCCAGGTCACTCTCCAGGGCCTCTCTAACCC 415 Var1 Basic-26 CGTCCGCGAGGGAGCCCGAGGGGTTAGAGAGGCCCTGGAG 416 Var1 Basic-27 CTCGGGCTCCCTCGCGGACGGCTCTGGTCTCGGCGAGCCC 417 Var1 Basic-28 TTCAGGGTCAACTCAAACTTGGGCTCGCCGAGACCAGAGC 418 Var1 Basic-29 AAGTTTGAGTTGACCCTGAAGCCTTTCACCGGCAACTGGG 419 Var1 Basic-30 GCCATCCCGCTGCGGTCGACCCCAGTTGCCGGTGAAAGGC 420 Var1 Basic-31 GTCGACCGCAGCGGGATGGCCCAGCTCTGCGAGCCATTGC 421 Var1 Basic-32 ACTTTGAGTATCCAATCAAGGCAATGGCTCGCAGAGCTGG 422 Var1 Basic-33 CTTGATTGGATACTCAAAGTGGCTCATCAACAACAACTAT 423 Var1 Basic-34 ACGTTGGACACAGTCGACTGATAGTTGTTGTTGATGAGCC 424 Var1 Basic-35 CAGTCGACTGTGTCCAACGTCATCTGGCCTATTGTGCGCA 425 Var1 Basic-36 GGCAACATAGTTGAGGTCGTTGCGCACAATAGGCCAGATG 426 Var1 Basic-37 ACGACCTCAACTATGTTGCCCAGTACTGGAACCAAACCGG 427 Var1 Basic-38 CTTCTTCCCAGAGGTCAAAGCCGGTTTGGTTCCAGTACTG 428 Var1 Basic-39 CTTTGACCTCTGGGAAGAAGTCAATGGGAGCTCATTCTTT 429 Var1 Basic-40 CGGTGCTGGTTGGCAACAGTAAAGAATGAGCTCCCATTGA 430 Var1 Basic-41 ACTGTTGCCAACCAGCACCGAGCACTTGTCGAGGGCGCCA 431 Var1 Basic-42 GCCAAGAGTGGCAGCAAGAGTGGCGCCCTCGACAAGTGCT 432 Var1 Basic-43 CTCTTGCTGCCACTCTTGGCCAGTCGGGAAGCGCTTATTC 433 Var1 Basic-44 AAACCTGGGGAGCAACAGATGAATAAGCGCTTCCCGACTG 434 Var1 Basic-45 ATCTGTTGCTCCCCAGGTTTTGTGCTTTCTCCAACGATTC 435 Var1 Basic-46 TATCCACCAGACGACACCCAGAATCGTTGGAGAAAGCACA 436 Var1 Basic-47 TGGGTGTCGTCTGGTGGATACGTCGACTCCAACATCAACA 437 Var1 Basic-48 GCCAGTCCTGCCCTCGTTGGTGTTGATGTTGGAGTCGACG 438 Var1 Basic-49 CCAACGAGGGCAGGACTGGCAAGGATGTCAACTCCGTCCT 439 Var1 Basic-50 CGAAGGTGTGGATGGAAGTCAGGACGGAGTTGACATCCTT 440 Var1 Basic-51 GACTTCCATCCACACCTTCGATCCCAACCTTGGCTGTGAC 441 Var1 Basic-52 CATGGCTGGAAGGTGCCTGCGTCACAGCCAAGGTTGGGAT 442 Var1 Basic-53 GCAGGCACCTTCCAGCCATGCAGTGACAAAGCGCTCTCCA 443 Var1 Basic-54 GTCGACAACAACCTTGAGGTTGGAGAGCGCTTTGTCACTG 444 Var1 Basic-55 ACCTCAAGGTTGTTGTCGACTCCTTCCGCTCCATCTACGG 445 Var1 Basic-56 CAGGAATGCCCTTGTTCACGCCGTAGATGGAGCGGAAGGA 446 Var1 Basic-57 CGTGAACAAGGGCATTCCTGCCGGTGCTGCCGTCGCCATT 447 Var1 Basic-58 ACATCCTCTGCATACCGGCCAATGGCGACGGCAGCACCGG 448 Var1 Basic-59 GGCCGGTATGCAGAGGATGTGTACTACAACGGCAACCCTT 449 Var1 Basic-60 AGCAAATGTAGCAAGATACCAAGGGTTGCCGTTGTAGTAC 450 Var1 Basic-61 GGTATCTTGCTACATTTGCTGCTGCCGAGCAGCTGTACGA 451 Var1 Basic-62 TCTTCCAGACGTAGATGGCATCGTACAGCTGCTCGGCAGC 452 Var1 Basic-63 TGCCATCTACGTCTGGAAGAAGACGGGCTCCATCACGGTG 453 Var1 Basic-64 AAGGCCAGGGAGGTGGCGGTCACCGTGATGGAGCCCGTCT 454 Var1 Basic-65 ACCGCCACCTCCCTGGCCTTCTTCCAGGAGCTTGTTCCTG 455 Var1 Basic-66 GTAGGTCCCGGCCGTCACGCCAGGAACAAGCTCCTGGAAG 456 Var1 Basic-67 GCGTGACGGCCGGGACCTACTCCAGCAGCTCTTCGACCTT 457 Var1 Basic-68 CGGCGTTGATGATGTTGGTAAAGGTCGAAGAGCTGCTGGA 458 Var1 Basic-69 TACCAACATCATCAACGCCGTCTCGACATACGCCGATGGC 459 Var1 Basic-70 TTGGCAGCCTCGCTGAGGAAGCCATCGGCGTATGTCGAGA 460 Var1 Basic-71 TTCCTCAGCGAGGCTGCCAAGTACGTCCCCGCCGACGGTT 461 Var1 Basic-72 GTCAAACTGCTCGGCCAGCGAACCGTCGGCGGGGACGTAC 462 Var1 Basic-73 CGCTGGCCGAGCAGTTTGACCGCAACAGCGGCACTCCGCT 463 Var1 Basic-74 ACGTCAGGTGAACCGCAGACAGCGGAGTGCCGCTGTTGCG 464 Var1 Basic-75 GTCTGCGGTTCACCTGACGTGGTCGTACGCCTCGTTCTTG 465 Var1 Basic-76 GCCCGACGAAGCGTGGCTGTCAAGAACGAGGCGTACGACC 466 Var1 Basic-77 ACAGCCACGCTTCGTCGGGCTGGCATCGTGCCCCCCTCGT 467 Var1 Basic-78 GCTAGCGCTGCTGTTGGCCCACGAGGGGGGCACGATGCCA 468 Var1 Basic-79 GGGCCAACAGCAGCGCTAGCACGATCCCCTCGACGTGCTC 469 Var1 Basic-80 ATCCGACCACGGACGCGCCGGAGCACGTCGAGGGGATCGT 470 Var1 Basic-81 CGGCGCGTCCGTGGTCGGATCCTACTCGCGTCCCACCGCC 471 Var1 Basic-82 TGCGACGGAGGGAATGACGTGGCGGTGGGACGCGAGTAGG 472 Var1 Basic-83 ACGTCATTCCCTCCGTCGCAGACGCCCAAGCCTGGCGTGC 473 Var1 Basic-84 CGTGTAGGGAGTACCGGAAGGCACGCCAGGCTTGGGCGTC 474 Var1 Basic-85 CTTCCGGTACTCCCTACACGCCCCTGCCCTGCGCGACCCC 475 Var1 Basic-86 AGGTGACGGCCACGGAGGTTGGGGTCGCGCAGGGCAGGGG 476 Var1 Basic-87 AACCTCCGTGGCCGTCACCTTCCACGAGCTCGTGTCGACA 477 Var1 Basic-88 TTGACCGTCTGGCCAAACTGTGTCGACACGAGCTCGTGGA 478 Var1 Basic-89 CAGTTTGGCCAGACGGTCAAGGTGGCGGGCAACGCCGCGG 479 Var1 Basic-90 CGTGCTCCAGTTGCCCAGGGCCGCGGCGTTGCCCGCCACC 480 Var1 Basic-91 CCCTGGGCAACTGGAGCACGAGCGCCGCCGTGGCTCTGGA 481 Var1 Basic-92 TATCACGATAGTTGACGGCGTCCAGAGCCACGGCGGCGCT 482 Var1 Basic-93 CGCCGTCAACTATCGTGATAACCACCCCCTGTGGATTGGG 483 Var1 Basic-94 CCAGCCTCGAGGTTGACCGTCCCAATCCACAGGGGGTGGT 484 Var1 Basic-95 ACGGTCAACCTCGAGGCTGGAGACGTCGTGGAGTACAAGT 485 Var1 Basic-96 ATCTTGGCCCACATTGATGTACTTGTACTCCACGACGTCT 486 Var1 Basic-97 ACATCAATGTGGGCCAAGATGGCTCCGTGACCTGGGAGAG 487 Var1 Basic-98 TGTAAGTGTGGTTGGGATCACTCTCCCAGGTCACGGAGCC 488 Var1 Basic-99 TGATCCCAACCACACTTACACGGTTCCTGCGGTGGCTTGT 489 Var1 Basic-100 TCCTTGACAACCTGCGTCACACAAGCCACCGCAGGAACCG 490 Var1 Basic-101 GTGACGCAGGTTGTCAAGGAGGACACCTGGCAGTCGTAAA 491 Var1 Basic-102 CTTTGTACAAGAAAGCTGGGTTTACGACTGCCAGGTGTCC 492 Var1 Basic-103 CCCAGCTTTCTTGTACAAAGTTGGCATTATAAGAAAGCAT 493 Var1 Basic-104 TTGCAACAAATTGATAAGCAATGCTTTCTTATAATGCCAA 494 Var1 Basic-105 TGCTTATCAATTTGTTGCAACGAACAGGTCACTATCAGTC 495 Var1 Basic-106 TCAAATAATGATTTTATTTTGACTGATAGTGACCTGTTCG 496 Var1 Basic-107 AAAATAAAATCATTATTTGAAGCTTAAGCCTGGGGTGCCT 497 Var1 Basic-108 AGAGAGTCATTAGGCACCCCAGGCTTAAGCT 498 Var2-18 GTAGTCCGGGTCTTGTGTGCTGGGAGATGCAATCACCGCA 499 Var2-19 GCACACAAGACCCGGACTACTATTACATGTGGACGCGAGA 500 Var3-21 TAGCGCTCTTGTCTTCAAGATTCTCATCGACCGCTTCACC 501 Var3-22 AGGCCCGCATCGTACGTTTCGGTGAAGCGGTCGATGAGAA 502 Var4-92 TATCACGATAGTTGACACGGTCCAGAGCCACGGCGGCGCT 503 Var4-93 CCGTGTCAACTATCGTGATAACCACCCCCTGTGGATTGGG 504 Var5-18 GTAGTCCGGGTCTTGTGTGCTGGGAGATGCAATCACCGCA 505 Var5-19 GCACACAAGACCCGGACTACTATTACATGTGGACGCGAGA 506 Var5-21 TAGCGCTCTTGTCTTCAAGATTCTCATCGACCGCTTCACC 507 Var5-22 AGGCCCGCATCGTACGTTTCGGTGAAGCGGTCGATGAGAA 508 Var6-21 TAGCGCTCTTGTCTTCAAGATTCTCATCGACCGCTTCACC 509 Var6-22 AGGCCCGCATCGTACGTTTCGGTGAAGCGGTCGATGAGAA 510 Var6-92 TATCACGATAGTTGACACGGTCCAGAGCCACGGCGGCGCT 511 Var6-93 CCGTGTCAACTATCGTGATAACCACCCCCTGTGGATTGGG 512 Var7-92 TATCACGATAGTTGACACGGTCCAGAGCCACGGCGGCGCT 513 Var7-93 CCGTGTCAACTATCGTGATAACCACCCCCTGTGGATTGGG 514 Var7-18 GTAGTCCGGGTCTTGTGTGCTGGGAGATGCAATCACCGCA 515 Var7-19 GCACACAAGACCCGGACTACTATTACATGTGGACGCGAGA 516 Var8-18 GTAGTCCGGGTCTTGTGTGCTGGGAGATGCAATCACCGCA 517 Var8-19 GCACACAAGACCCGGACTACTATTACATGTGGACGCGAGA 518 Var8-21 TAGCGCTCTTGTCTTCAAGATTCTCATCGACCGCTTCACC 519 Var8-22 AGGCCCGCATCGTACGTTTCGGTGAAGCGGTCGATGAGAA 520 Var8-92 TATCACGATAGTTGACACGGTCCAGAGCCACGGCGGCGCT 521 Var8-93 CCGTGTCAACTATCGTGATAACCACCCCCTGTGGATTGGG 522 Var9-18 GTAGTCCGGGTCTTGTGTGCTGGGAGATGCAATCACCGCA 523 Var9-19 GCACACAAGACCCGGACTACTATTACATGTGGACGCGAGA 524 Var9-21 TAGCGCTCTTGTCTTCAAGATTCTCATCGACCGCTTCACC 525 Var9-22 AGGCCCGCATCGTACGTTTCGGTGAAGCGGTCGATGAGAA 526 Var9-92 TATCACGATAGTTGACACGGTCCAGAGCCACGGCGGCGCT 527 Var9-93 CCGTGTCAACTATCGTGATAACCACCCCCTGTGGATTGGG 528 Var9-76 GCCCGACGAAGAGCGGCTGTCAAGAACGAGGCGTACGACC 529 Var9-77 ACAGCCGCTCTTCGTCGGGCTGGCATCGTGCCCCCCTCGT 530 Var10-76 GCCCGACGAAGAGCGGCTGTCAAGAACGAGGCGTACGACC 531 Var10-77 ACAGCCGCTCTTCGTCGGGCTGGCATCGTGCCCCCCTCGT 532 Var10-88 TTGACCGTATGGCCAAACTGTGTCGACACGAGCTCGTGGA 533 Var10-89 CAGTTTGGCCATACGGTCAAGGTGGCGGGCAACGCCGCGG 534 Var10-92 TATCACGATAGTTGACACGGTCCAGAGCCACGGCGGCGCT 535 Var10-93 CCGTGTCAACTATCGTGATAACCACCCCCTGTGGATTGGG 536 Var10-96 ATCTTGGCCCACAATGATGTACTTGTACTCCACGACGTCT 537 Var10-97 ACATCATTGTGGGCCAAGATGGCTCCGTGACCTGGGAGAG 538 Var10-18 GTAGTCCGGGTCTTGTGTGCTGGGAGATGCAATCACCGCA 539 Var10-19 GCACACAAGACCCGGACTACTATTACATGTGGACGCGAGA 540 Var11-76 GCCCGACGAAGAGCGGCTGTCAAGAACGAGGCGTACGACC 541 Var11-77 ACAGCCGCTCTTCGTCGGGCTGGCATCGTGCCCCCCTCGT 542 Var11-88 TTGACCGTATGGCCAAACTGTGTCGACACGAGCTCGTGGA 543 Var1l-89 CAGTTTGGCCATACGGTCAAGGTGGCGGGCAACGCCGCGG 544 Var1l-92 TATCACGATAGTTGACACGGTCCAGAGCCACGGCGGCGCT 545 Var1l-93 CCGTGTCAACTATCGTGATAACCACCCCCTGTGGATTGGG 546 Var1l-96 ATCTTGGCCCACAATGATGTACTTGTACTCCACGACGTCT 547 Var11-97 ACATCATTGTGGGCCAAGATGGCTCCGTGACCTGGGAGAG 548 Var11-21 TAGCGCTCTTGTCTTCAAGATTCTCATCGACCGCTTCACC 549 Var1l-22 AGGCCCGCATCGTACGTTTCGGTGAAGCGGTCGATGAGAA 550 Var12-76 GCCCGACGAAGAGCGGCTGTCAAGAACGAGGCGTACGACC 551 Var12-77 ACAGCCGCTCTTCGTCGGGCTGGCATCGTGCCCCCCTCGT 552 Var12-88 TTGACCGTATGGCCAAACTGTGTCGACACGAGCTCGTGGA 553 Var12-89 CAGTTTGGCCATACGGTCAAGGTGGCGGGCAACGCCGCGG 554 Var12-92 TATCACGATAGTTGACACGGTCCAGAGCCACGGCGGCGCT 555 Var12-93 CCGTGTCAACTATCGTGATAACCACCCCCTGTGGATTGGG 556 Var12-96 ATCTTGGCCCACAATGATGTACTTGTACTCCACGACGTCT 557 Var12-97 ACATCATTGTGGGCCAAGATGGCTCCGTGACCTGGGAGAG 558 Var12-18 GTAGTCCGGGTCTTGTGTGCTGGGAGATGCAATCACCGCA 559 Var12-19 GCACACAAGACCCGGACTACTATTACATGTGGACGCGAGA 560 Var12-21 TAGCGCTCTTGTCTTCAAGATTCTCATCGACCGCTTCACC 561 Var12-22 AGGCCCGCATCGTACGTTTCGGTGAAGCGGTCGATGAGAA 562 Var13-18 GTAGTCCGGGTCACGTGTGCTGGGAGATGCAATCACCGCA 563 Var13-19 GCACACGTGACCCGGACTACTATTACATGTGGACGCGAGA 564 Var14-18 GTAGTCCGGGTCACGTGTGCTGGGAGATGCAATCACCGCA 565 Var14-19 GCACACGTGACCCGGACTACTATTACATGTGGACGCGAGA 566 Var14-21 TAGCGCTCTTGTCTTCAAGATTCTCATCGACCGCTTCACC 567 Var14-22 AGGCCCGCATCGTACGTTTCGGTGAAGCGGTCGATGAGAA 568 Var15-18 GTAGTCCGGGTCACGTGTGCTGGGAGATGCAATCACCGCA 569 Var15-19 GCACACGTGACCCGGACTACTATTACATGTGGACGCGAGA 570 Var15-21 TAGCGCTCTTGTCTTCAAGATTCTCATCGACCGCTTCACC 571 Var15-22 AGGCCCGCATCGTACGTTTCGGTGAAGCGGTCGATGAGAA 572 Var15-92 TATCACGATAGTTGACACGGTCCAGAGCCACGGCGGCGCT 573 Var15-93 CCGTGTCAACTATCGTGATAACCACCCCCTGTGGATTGGG 574 Var15-76 GCCCGACGAAGAGCGGCTGTCAAGAACGAGGCGTACGACC 575 Var15-77 ACAGCCGCTCTTCGTCGGGCTGGCATCGTGCCCCCCTCGT 576 Var16-74 ACGTCAGGTGACGCGCAGACAGCGGAGTGCCGCTGTTGCG 577 Var16-75 GTCTGCGCGTCACCTGACGTGGTCGTACGCCTCGTTCTTG 578 Var17-74 ACGTCAGGTGACCCGCAGACAGCGGAGTGCCGCTG1TGCG 579 Var17-75 GTCTGCGGGTCACCTGACGTGGTCGTACGCCTCGTTCTTG 580 Var18-22 AGAAACGCATCGTACGTTTCGGTGAAGCGGTCGATGAGGT 581 Var18-23 GAAACGTACGATGCGTTTCTGCAGCGCCGCATCGAGCAGT 582 Var18-74 ACGTCAGGTGACGCGCAGACAGCGGAGTGCCGCTGTTGCG 583 Var18-75 GTCTGCGCGTCACCTGACGTGGTCGTACGCCTCGTTCTTG 584 Var18-76 GCCCGACGGGCCGTGGCTGTCAAGAACGAGGCGTACGACC 585 Var18-77 ACAGCCACGGCCCGTCGGGCTGGCATCGTGCCCCCCTCGT 586 Var18-87 AACCTCCGTGGCCGTCACCTTCCACGTTCTCGTGTCGACA 587 Var18-88 TTGACCGTCTGGCCAAACTGTGTCGACACGAGAACGTGGA 588 Var18-96 ATCTTGGCCCACTTTGATGTACTTGTACTCCACGACGTCT 589 Var18-97 ACATCAAAGTGGGCCAAGATGGCTCCGTGACCTGGGAGAG 590 Var19-18 GTAGTCCGGGTCACGTGTGCTGGGAGATGCAATCACCGCA 591 Var19-19 GCACACGTGACCCGGACTACTATTACATGTGGACGCGAGA 592 Var19-22 AGAAACGCATCGTACGTTTCGGTGAAGCGGTCGATGAGGT 593 Var19-23 GAAACGTACGATGCGTTTCTGCAGCGCCGCATCGAGCAGT 594 Var19-74 ACGTCAGGTGACGCGCAGACAGCGGAGTGCCGCTGTTGCG 595 Var19-75 GTCTGCGCGTCACCTGACGTGGTCGTACGCCTCGTTCTTG 596 Var19-76 GCCCGACGGGCCGTGGCTGTCAAGAACGAGGCGTACGACC 597 Var19-77 ACAGCCACGGCCCGTCGGGCTGGCATCGTGCCCCCCTCGT 598 Var19-87 AACCTCCGTGGCCGTCACCTTCCACGTTCTCGTGTCGACA 599 Var19-88 TTGACCGTCTGGCCAAACTGTGTCGACACGAGAACGTGGA 600 Var19-96 ATCTTGGCCCACTTTGATGTACTTGTACTCCACGACGTCT 601 Var19-97 ACATCAAAGTGGGCCAAGATGGCTCCGTGACCTGGGAGAG 602 Var20-18 GTAGTCCGGGTCACGTGTGCTGGGAGATGCAATCACCGCA 603 Var20-19 GCACACGTGACCCGGACTACTATTACATGTGGACGCGAGA 604 Var20-22 AGAAACGCATCGTACGTTTCGGTGAAGCGGTCGATGAGGT 605 Var20-23 GAAACGTACGATGCGTTTCTGCAGCGCCGCATCGAGCAGT 606 Var20-74 ACGTCAGGTGAAGCGCAGACAGCGGAGTGCCGCTGTTGCG 607 Var20-75 GTCTGCGCTTCACCTGACGTGGTCGTACGCCTCGTTCTTG 608 Var20-76 GCCCGACGGGCCGTGGCTGTCAAGAACGAGGCGTACGACC 609 Var20-77 ACAGCCACGGCCCGTCGGGCTGGCATCGTGCCCCCCTCGT 610 Var20-87 AACCTCCGTGGCCGTCACCTTCCACGTTCTCGTGTCGACA 611 Var20-88 TTGACCGTATGGCCAAACTGTGTCGACACGAGAACGTGGA 612 Var20-89 CAGTTTGGCCATACGGTCAAGGTGGCGGGCAACGCCGCGG 613 Var20-93 TATCGGCATAGTTGACGGCGTCCAGAGCCACGGCGGCGCT 614 Var20-94 CGCCGTCAACTATGCCGATAACCACCCCCTGTGGATTGGG 615 Var20-96 ATCTTGGCCCACTTTGATGTACTTGTACTCCACGACGTCT 616 Var20-97 ACATCAAAGTGGGCCAAGATGGCTCCGTGACCTGGGAGAG 617 GAV Basic-1 ACAAGTTTGTACAAAAAAGCAGGCT 618 GAV Basic-2 GCAGTCGACAGGACGTGCATAGCCTGCTTTTTTGTACAAA 619 GAV Basic-3 ATGCACGTCCTGTCGACTGCGGTGCTGCTCGGCTCCGTTG 620 GAV Basic-4 TCCCAGGACCTTTTGAACGGCAACGGAGCCGAGCAGCACC 621 GAV Basic-5 CCGTTCAAAAGGTCCTGGGAAGACCAGGATCAAGCGGTCT 622 GAV Basic-6 ACCTCTTGGTGACGTCGGACAGACCGCTTGATCCTGGTCT 623 GAV Basic-7 GTCCGACGTCACCAAGAGGTCTGTTGACGACTTCATCAGC 624 GAV Basic-8 AGTGCAATAGGCGTCTCGGTGCTGATGAAGTCGTCAACAG 625 GAV Basic-9 ACCGAGACGCCTATTGCACTGAACAATCTTCTTTGCAATG 626 GAV Basic-10 ACGGCATCCATCAGGACCAACATTGCAAAGAAGATTGTTC 627 GAV Basic-11 TTGGTCCTGATGGATGCCGTGCATTCGGCACATCAGCTGG 628 GAV Basic-12 TGGGAGATGCAATCACCGCACCAGCTGATGTGCCGAATGC 629 GAV Basic-13 TGCGGTGATTGCATCTCCCAGCACAATTGACCCGGACTAC 630 GAV Basic-14 TCTCGCGTCCACATGTAATAGTAGTCCGGGTCAATTGTGC 631 GAV Basic-15 TATTACATGTGGACGCGAGATAGCGCTCTTGTCTTCAAGA 632 GAV Basic-16 GGTGAAGCGGTCGATGAGGTTCTTGAAGACAAGAGCGCTA 633 GAV Basic-17 ACCTCATCGACCGCTTCACCGAAACGTACGATGCGGGCCT 634 GAV Basic-18 ACTGCTCGATGCGGCGCTGCAGGCCCGCATCGTACGTTTC 635 GAV Basic-19 GCAGCGCCGCATCGAGCAGTACATTACTGCCCAGGTCACT 636 GAV Basic-20 GGGTTAGAGAGGCCCTGGAGAGTGACCTGGGCAGTAATGT 637 GAV Basic-21 CTCCAGGGCCTCTCTAACCCCTCGGGCTCCCTCGCGGACG 638 GAV Basic-22 GGGCTCGCCGAGACCAGAGCCGTCCGCGAGGGAGCCCGAG 639 GAV Basic-23 GCTCTGGTCTCGGCGAGCCCAAGTTTGAGTTGACCCTGAA 640 GAV Basic-24 CCCAGTTGCCGGTGAAAGGCTTCAGGGTCAACTCAAACTT 641 GAV Basic-25 GCCTTTCACCGGCAACTGGGGTCGACCGCAGCGGGATGGC 642 GAV Basic-26 GCAATGGCTCGCAGAGCTGGGCCATCCCGCTGCGGTCGAC 643 GAV Basic-27 CCAGCTCTGCGAGCCATTGCCTTGATTGGATACTCAAAGT 644 GAV Basic-28 ATAGTTGTTGTTGATGAGCCACTTTGAGTATCCAATCAAG 645 GAV Basic-29 GGCTCATCAACAACAACTATCAGTCGACTGTGTCCAACGT 646 GAV Basic-30 TGCGCACAATAGGCCAGATGACGTTGGACACAGTCGACTG 647 GAV Basic-31 CATCTGGCCTATTGTGCGCAACGACCTCAACTATGTTGCC 648 GAV Basic-32 CCGGTTTGGTTCCAGTACTGGGCAACATAGTTGAGGTCGT 649 GAV Basic-33 CAGTACTGGAACCAAACCGGCTTTGACCTCTGGGAAGAAG 650 GAV Basic-34 AAAGAATGAGCTCCCATTGACTTCTTCCCAGAGGTCAAAG 651 GAV Basic-35 TCAATGGGAGCTCATTCTTTACTGTTGCCAACCAGCACCG 652 GAV Basic-36 TGGCGCCCTCGACAAGTGCTCGGTGCTGGTTGGCAACAGT 653 GAV Basic-37 AGCACTTGTCGAGGGCGCCACTCTTGCTGCCACTCTTGGC 654 GAV Basic-38 GAATAAGCGCTTCCCGACTGGCCAAGAGTGGCAGCAAGAG 655 GAV Basic-39 CAGTCGGGAAGCGCTTATTCATCTGTTGCTCCCCAGGTTT 656 GAV Basic-40 GAATCGTTGGAGAAAGCACAAAACCTGGGGAGCAACAGAT 657 GAV Basic-41 TGTGCTTTCTCCAACGATTCTGGGTGTCGTCTGGTGGATA 658 GAV Basic-42 TGTTGATGTTGGAGTCGACGTATCCACCAGACGACACCCA 659 GAV Basic-43 CGTCGACTCCAACATCAACACCAACGAGGGCAGGACTGGC 660 GAV Basic-44 AGGACGGAGTTGACATCCTTGCCAGTCCTGCCCTCGTTGG 661 GAV Basic-45 AAGGATGTCAACTCCGTCCTGACTTCCATCCACACCTTCG 662 GAV Basic-46 GTCACAGCCAAGGTTGGGATCGAAGGTGTGGATGGAAGTC 663 GAV Basic-47 ATCCCAACCTTGGCTGTGACGCAGGCACCTTCCAGCCATG 664 GAV Basic-48 TGGAGAGCGCTTTGTCACTGCATGGCTGGAAGGTGCCTGC 665 GAV Basic-49 CAGTGACAAAGCGCTCTCCAACCTCAAGGTTGTTGTCGAC 666 GAV Basic-50 CCGTAGATGGAGCGGAAGGAGTCGACAACAACCTTGAGGT 667 GAV Basic-51 TCCTTCCGCTCCATCTACGGCGTGAACAAGGGCATTCCTG 668 GAV Basic-52 AATGGCGACGGCAGCACCGGCAGGAATGCCCTTGTTCACG 669 GAV Basic-53 CCGGTGCTGCCGTCGCCATTGGCCGGTATGCAGAGGATGT 670 GAV Basic-54 AAGGGTTGCCGTTGTAGTACACATCCTCTGCATACCGGCC 671 GAV Basic-55 GTACTACAACGGCAACCCTTGGTATCTTGCTACATTTGCT 672 GAV Basic-56 TCGTACAGCTGCTCGGCAGCAGCAAATGTAGCAAGATACC 673 GAV Basic-57 GCTGCCGAGCAGCTGTACGATGCCATCTACGTCTGGAAGA 674 GAV Basic-58 CACCGTGATGGAGCCCGTCTTCTTCCAGACGTAGATGGCA 675 GAV Basic-59 AGACGGGCTCCATCACGGTGACCGCCACCTCCCTGGCCTT 676 GAV Basic-60 CAGGAACAAGCTCCTGGAAGAAGGCCAGGGAGGTGGCGGT 677 GAV Basic-61 CTTCCAGGAGCTTGTTCCTGGCGTGACGGCCGGGACCTAC 678 GAV Basic-62 AAGGTCGAAGAGCTGCTGGAGTAGGTCCCGGCCGTCACGC 679 GAV Basic-63 TCCAGCAGCTCTTCGACCTTTACCAACATCATCAACGCCG 680 GAV Basic-64 GCCATCGGCGTATGTCGAGACGGCGTTGATGATGTTGGTA 681 GAV Basic-65 TCTCGACATACGCCGATGGCTTCCTCAGCGAGGCTGCCAA 682 GAV Basic-66 AACCGTCGGCGGGGACGTACTTGGCAGCCTCGCTGAGGAA 683 GAV Basic-67 GTACGTCCCCGCCGACGGTTCGCTGGCCGAGCAGTTTGAC 684 GAV Basic-68 AGCGGAGTGCCGCTGTTGCGGTCAAACTGCTCGGCCAGCG 685 GAV Basic-69 CGCAACAGCGGCACTCCGCTGTCTGCGCTTCACCTGACGT 686 GAV Basic-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAAGCGCAGAC 687 GAV Basic-71 GGTCGTACGCCTCGTTCTTGACAGCCACGGCCCGTCGGGC 688 GAV Basic-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCGTGGCTGT 689 GAV Basic-73 TGGCATCGTGCCCCCCTCGTGGGCCAACAGCAGCGCTAGC 690 GAV Basic-74 GAGCACGTCGAGGGGATCGTGCTAGCGCTGCTGTTGGCCC 691 GAV Basic-75 ACGATCCCCTCGACGTGCTCCGGCGCGTCCGTGGTCGGAT 692 GAV Basic-76 GGCGGTGGGACGCGAGTAGGATCCGACCACGGACGCGCCG 693 GAV Basic-77 CCTACTCGCGTCCCACCGCCACGTCATTCCCTCCGTCGCA 694 GAV Basic-78 GCACGCCAGGCTTGGGCGTCTGCGACGGAGGGAATGACGT 695 GAV Basic-79 GACGCCCAAGCCTGGCGTGCCTTCCGGTACTCCCTACACG 696 GAV Basic-80 GGGGTCGCGCAGGGCAGGGGCGTGTAGGGAGTACCGGAAG 697 GAV Basic-81 CCCCTGCCCTGCGCGACCCCAACCTCCGTGGCCGTCACCT 698 GAV Basic-82 TGTCGACACGAGCTCGTGGAAGGTGACGGCCACGGAGGTT 699 GAV Basic-83 TCCACGAGCTCGTGTCGACACAGTTTGGCCAGACGGTCAA 700 GAV Basic-84 CCGCGGCGTTGCCCGCCACCTTGACCGTCTGGCCAAACTG 701 GAV Basic-85 GGTGGCGGGCAACGCCGCGGCCCTGGGCAACTGGAGCACG 702 GAV Basic-86 TCCAGAGCCACGGCGGCGCTCGTGCTCCAGTTGCCCAGGG 703 GAV Basic-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATGCCGATA 704 GAV Basic-88 CCCAATCCACAGGGGGTGGTTATCGGCATAGTTGACGGCG 705 GAV Basic-89 ACCACCCCCTGTGGATTGGGACGGTCAACCTCGAGGCTGG 706 GAV Basic-90 ACTTGTACTCCACGACGTCTCCAGCCTCGAGGTTGACCGT 707 GAV Basic-91 AGACGTCGTGGAGTACAAGTACATCAATGTGGGCCAAGAT 708 GAV Basic-92 CTCTCCCAGGTCACGGAGCCATCTTGGCCCACATTGATGT 709 GAV Basic-93 GGCTCCGTGACCTGGGAGAGTGATCCCAACCACACTTACA 710 GAV Basic-94 ACAAGCCACCGCAGGAACCGTGTAAGTGTGGTTGGGATCA 711 GAV Basic-95 CGGTTCCTGCGGTGGCTTGTGTGACGCAGGTTGTCAAGGA 712 GAV Basic-96 TTTACGACTGCCAGGTGTCCTCCTTGACAACCTGCGTCAC 713 GAV Basic-97 GGACACCTGGCAGTCGTAAACCCAGCTTTCTTGTACAAAG 714 GAV Basic-98 ACCACTTTGTACAAGAAAGCTGGG 715 All1-13 TGCGGTGATTGCATCTCCCAGCACACTTTGCCCGGACTAC 716 All1-14 TCTCGCGTCCACATGTAATAGTAGTCCGGGCAAAGTGTGC 717 All1-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 718 All1-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 719 All1-82 TGTCGACACGAGCGCGTGGAAGGTGACGGCCACGGAGGTT 720 All1-83 TCCACGCGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 721 All1-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 722 All1-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATAGAGATA 723 All1-88 CCCAATCCACAGGGGGTGGTTATCTCTATAGTTGACGGCG 724 All2-13 TGCGGTGATTGCATCTCCCAGCACACTTGACCCGGACTAC 725 All2-14 TCTCGCGTCCACATGTAATAGTAGTCCGGGTCAAGTGTGC 726 All2-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 727 All2-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 728 All2-82 TGTCGACACGAGCGCGTGGAAGGTGACGGCCACGGAGGTT 729 All2-83 TCCACGCGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 730 All2-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 731 All2-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATAGAGATA 732 All2-88 CCCAATCCACAGGGGGTGGTTATCTCTATAGTTGACGGCG 733 All3-13 TGCGGTGATTGCATCTCCCAGCACACTTTGCCCGGACTAC 734 All3-14 TCTCGCGTCCACATGTAATAGTAGTCCGGGCAAAGTGTGC 735 All3-16 GGTGAAGCGGTCGATGAGGATCTTGAAGACAAGAGCGCTA 736 All3-17 TCCTCATCGACCGCTTCACCGAAACGTACGATGCGGGCCT 737 All3-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 738 All3-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 739 All3-82 TGTCGACACGAGCGCGTGGAAGGTGACGGCCACGGAGGTT 740 All3-83 TCCACGCGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 741 All3-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 742 All3-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATAGAGATA 743 All3-88 CCCAATCCACAGGGGGTGGTTATCTCTATAGTTGACGGCG 744 All4-13 TGCGGTGATTGCATCTCCCAGCACACTTGACCCGGACTAC 745 All4-14 TCTCGCGTCCACATGTAATAGTAGTCCGGGTCAAGTGTGC 746 All4-16 GGTGAAGCGGTCGATGAGGATCTTGAAGACAAGAGCGCTA 747 All4-17 TCCTCATCGACCGCTTCACCGAAACGTACGATGCGGGCCT 748 All4-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 749 All4-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 750 All4-82 TGTCGACACGAGCGCGTGGAAGGTGACGGCCACGGAGGTT 751 All4-83 TCCACGCGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 752 All4-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 753 All4-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATAGAGATA 754 All4-88 CCCAATCCACAGGGGGTGGTTATCTCTATAGTTGACGGCG 755 All5-13 TGCGGTGATTGCATCTCCCAGCACAAGAGACCCGGACTAC 756 All5-14 TCTCGCGTCCACATGTAATAGTAGTCCGGGTCTCTTGTGC 757 All5-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 758 All5-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 759 All5-82 TGTCGACACGAGCGCGTGGAAGGTGACGGCCACGGAGGTT 760 All5-83 TCCACGCGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 761 All5-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 762 All5-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATAGAGATA 763 All5-88 CCCAATCCACAGGGGGTGGTTATCTCTATAGTTGACGGCG 764 All6-13 TGCGGTGATTGCATCTCCCAGCACAAGAGACCCGGACTAC 765 All6-14 TCTCGCGTCCACATGTAATAGTAGTCCGGGTCTCTTGTGC 766 All6-16 GGTGAAGCGGTCGATGAGGATCTTGAAGACAAGAGCGCTA 767 All6-17 TCCTCATCGACCGCTTCACCGAAACGTACGATGCGGGCCT 768 All6-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 769 All6-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 770 All6-82 TGTCGACACGAGCGCGTGGAAGGTGACGGCCACGGAGGTT 771 All6-83 TCCACGCGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 772 All6-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 773 All6-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATAGAGATA 774 All6-88 CCCAATCCACAGGGGGTGGTTATCTCTATAGTTGACGGCG 775 All7-13 TGCGGTGATTGCATCTCCCAGCACAAGAGACCCGGACTAC 776 All7-14 TCTCGCGTCCACATGTAATAGTAGTCCGGGTCTCTTGTGC 777 All7-69 CGCAACAGCGGCACTCCGCTGTCTGCGAGACACCTGACGT 778 All7-70 CAAGAACGAGGCGTACGACCACGTCAGGTGTCTCGCAGAC 779 All7-82 TGTCGACACGAGCGCGTGGAAGGTGACGGCCACGGAGGTT 780 All7-83 TCCACGCGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 781 All7-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 782 All7-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATAGAGATA 783 All7-88 CCCAATCCACAGGGGGTGGTTATCTCTATAGTTGACGGCG 784 All8-13 TGCGGTGATTGCATCTCCCAGCACAAGAGACCCGGACTAC 785 All8-14 TCTCGCGTCCACATGTAATAGTAGTCCGGGTCTCTTGTGC 786 All8-16 GGTGAAGCGGTCGATGAGGATCTTGAAGACAAGAGCGCTA 787 All8-17 TCCTCATCGACCGCTTCACCGAAACGTACGATGCGGGCCT 788 All8-69 CGCAACAGCGGCACTCCGCTGTCTGCGAGACACCTGACGT 789 All8-70 CAAGAACGAGGCGTACGACCACGTCAGGTGTCTCGCAGAC 790 All8-82 TGTCGACACGAGCGCGTGGAAGGTGACGGCCACGGAGGTT 791 All8-83 TCCACGCGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 792 All8-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 793 All8-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATAGAGATA 794 All8-88 CCCAATCCACAGGGGGTGGTTATCTCTATAGTTGACGGCG 795 CS1-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 796 CS1-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 797 CS1-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGCTCCGTCGGGC 798 CS1-72 ACGAGGGGGGCACGATGCCAGCCCGACGGAGCGCGGCTGT 799 CS1-83 TCCACGAGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 800 CS1-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 801 CS1-87 AGCGCCGCCGTGGCTCTGGACCGCGTCAACTATCGCGATA 802 CS1-88 CCCAATCCACAGGGGGTGGTTATCGCGATAGTTGACGCGG 803 CS1-91 AGACGTCGTGGAGTACAAGTACATCATTGTGGGCCAAGAT 804 CS1-92 CTCTCCCAGGTCACGGAGCCATCTTGGCCCACAATGATGT 805 CS2-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 806 CS2-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 807 CS2-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGCAACGTCGGGC 808 CS2-72 ACGAGGGGGGCACGATGCCAGCCCGACGTTGCGCGGCTGT 809 CS2-83 TCCACGAGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 810 CS2-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 811 CS2-87 AGCGCCGCCGTGGCTCTGGACCGCGTCAACTATCGCGATA 812 CS2-88 CCCAATCCACAGGGGGTGGTTATCGCGATAGTTGACGCGG 813 CS2-91 AGACGTCGTGGAGTACAAGTACATCATTGTGGGCCAAGAT 814 CS2-92 CTCTCCCAGGTCACGGAGCCATCTTGGCCCACAATGATGT 815 CS3-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 816 CS3-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 817 CS3-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGGCCCGTCGGGC 818 CS3-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCGCGGCTGT 819 CS3-83 TCCACGAGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 820 CS3-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 821 CS3-87 AGCGCCGCCGTGGCTCTGGACCGCGTCAACTATGCCGATA 822 CS3-88 CCCAATCCACAGGGGGTGGTTATCGGCATAGTTGACGCGG 823 CS3-91 AGACGTCGTGGAGTACAAGTACATCATTGTGGGCCAAGAT 824 CS3-92 CTCTCCCAGGTCACGGAGCCATCTTGGCCCACAATGATGT 825 CS4-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 826 CS4-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 827 CS4-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGGCCCGTCGGGC 828 CS4-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCGCGGCTGT 829 CS4-83 TCCACGAGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 830 CS4-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 831 CS4-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATCGCGATA 832 CS4-88 CCCAATCCACAGGGGGTGGTTATCGCGATAGTTGACGGCG 833 CS4-91 AGACGTCGTGGAGTACAAGTACATCATTGTGGGCCAAGAT 834 CS4-92 CTCTCCCAGGTCACGGAGCCATCTTGGCCCACAATGATGT 835 LQ1-50 CAGTAGATGGAGCGGAAGGAGTCGACAACAACCTTGAGGT 836 LQ1-51 TCCTTCCGCTCCATCTACTGCGTGAACAAGGGCATTCCTG 837 LQ1-69 CGCAACAGCGGCACTCCGCTGTCTGCGAGACACCTGACGT 838 LQ1-70 CAAGAACGAGGCGTACGACCACGTCAGGTGTCTCGCAGAC 839 LQ1-71 GGTCGTACGCCTCGTTCTTGACAGCCACGCTCCGTCGGGC 840 LQ1-72 ACGAGGGGGGCACGATGCCAGCCCGACGGAGCGTGGCTGT 841 LQ2-50 CAGTAGATGGAGCGGAAGGAGTCGACAACAACCTTGAGGT 842 LQ2-51 TCCTTCCGCTCCATCTACTGCGTGAACAAGGGCATTCCTG 843 LQ2-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTACACCTGACGT 844 LQ2-70 CAAGAACGAGGCGTACGACCACGTCAGGTGTACCGCAGAC 845 LQ2-71 GGTCGTACGCCTCGTTCTTGACAGCCACGCAGCGTCGGGC 846 LQ2-72 ACGAGGGGGGCACGATGCCAGCCCGACGCTGCGTGGCTGT 847 LQ3-50 CAGTAGATGGAGCGGAAGGAGTCGACAACAACCTTGAGGT 848 LQ3-51 TCCTTCCGCTCCATCTACTGCGTGAACAAGGGCATTCCTG 849 LQ3-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTACACCTGACGT 850 LQ3-70 CAAGAACGAGGCGTACGACCACGTCAGGTGTACCGCAGAC 851 LQ3-71 GGTCGTACGCCTCGTTCTTGACAGCCACGTTACGTCGGGC 852 LQ3-72 ACGAGGGGGGCACGATGCCAGCCCGACGTAACGTGGCTGT 853 LQ3-83 TCCACGAGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 854 LQ3-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 855 LQ4-50 CAGTAGATGGAGCGGAAGGAGTCGACAACAACCTTGAGGT 856 LQ4-51 TCCTTCCGCTCCATCTACTGCGTGAACAAGGGCATTCCTG 857 LQ4-69 CGCAACAGCGGCACTCCGCTGTCTGCGAGACACCTGACGT 858 LQ4-70 CAAGAACGAGGCGTACGACCACGTCAGGTGTCTCGCAGAC 859 LQ4-71 GGTCGTACGCCTCGTTCTTGACAGCCACGCAGCGTCGGGC 860 LQ4-72 ACGAGGGGGGCACGATGCCAGCCCGACGCTGCGTGGCTGT 861 LQ4-83 TCCACGAGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 862 LQ4-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 863 LQ5-69 CGCAACAGCGGCACTCCGCTGTCTGCGCGTCACCTGACGT 864 LQ5-70 CAAGAACGAGGCGTACGACCACGTCAGGTGACGCGCAGAC 865 LQ5-71 GGTCGTACGCCTCGTTCTTGACAGCCACGCTCCGTCGGGC 866 LQ5-72 ACGAGGGGGGCACGATGCCAGCCCGACGGAGCGTGGCTGT 867 LQ5-83 TCCACGAGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 868 LQ5-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 869 LQ6-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 870 LQ6-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 871 LQ6-71 GGTCGTACGCCTCGTTCTTGACAGCCACGCTTCGTCGGGC 872 LQ6-72 ACGAGGGGGGCACGATGCCAGCCCGACGAAGCGTGGCTGT 873 LQ6-83 TCCACGAGCTCGTGTCGACACAGTTTGGCCATACGGTCAA 874 LQ6-84 CCGCGGCGTTGCCCGCCACCTTGACCGTATGGCCAAACTG 875 TS1-13 TGCGGTGATTGCATCTCCCAGCACAAGAGACCCGGACTAC 876 TS1-14 TCTCGCGTCCACATGTAATAGTAGTCCGGGTCTCTTGTGC 877 TS1-71 GGTCGTACGCCTCGTTCTTGACAGCCGCAGCCCGTCGGGC 878 TS1-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCTGCGGCTGT 879 TS1-82 TGTCGACACGAGCACGTGGAAGGTGACGGCCACGGAGGTT 880 TS1-83 TCCACGTGCTCGTGTCGACACAGTTTGGCCAGACGGTCAA 881 TS1-87 AGCGCCGCCGTGGCTCTGGACCGCGTCAACTATGCCGATA 882 TS1-88 CCCAATCCACAGGGGGTGGTTATCGGCATAGTTGACGCGG 883 TS1-91 AGACGTCGTGGAGTACAAGTACATCAAAGTGGGCCAAGAT 884 TS1-92 CTCTCCCAGGTCACGGAGCCATCTTGGCCCACTTTGATGT 885 TS2-13 TGCGGTGATTGCATCTCCCAGCACAATTAGACCGGACTAC 886 TS2-14 TCTCGCGTCCACATGTAATAGTAGTCCGGTCTAATTGTGC 887 TS2-82 TGTCGACACGAGCGCGTGGAAGGTGACGGCCACGGAGGTT 888 TS2-83 TCCACGCGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 889 TS2-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 890 TS2-91 AGACGTCGTGGAGTACAAGTACATCATTGTGGGCCAAGAT 891 TS2-92 CTCTCCCAGGTCACGGAGCCATCTTGGCCCACAATGATGT 892 TS3-82 TGTCGACACGAGCGCGTGGAAGGTGACGGCCACGGAGGTT 893 TS3-83 TCCACGCGCTCGTGTCGACACAGTTTGGCCAGACGGTCAA 894 TS3-91 AGACGTCGTGGAGTACAAGTACATCATTGTGGGCCAAGAT 895 TS3-92 CTCTCCCAGGTCACGGAGCCATCTTGGCCCACAATGATGT 896 TS4-13 TGCGGTGATTGCATCTCCCAGCACAAGAGACCCGGACTAC 897 TS4-14 TCTCGCGTCCACATGTAATAGTAGTCCGGGTCTCTTGTGC 898 TS4-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGGCCCGTCGGGC 899 TS4-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCGCGGCTGT 900 TS4-82 TGTCGACACGAGCGCGTGGAAGGTGACGGCCACGGAGGTT 901 TS4-83 TCCACGCGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 902 TS4-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 903 TS4-91 AGACGTCGTGGAGTACAAGTACATCATTGTGGGCCAAGAT 904 TS4-92 CTCTCCCAGGTCACGGAGCCATCTTGGCCCACAATGATGT 905 TS5-13 TGCGGTGATTGCATCTCCCAGCACAATTCGCCCGGACTAC 906 TS5-14 TCTCGCGTCCACATGTAATAGTAGTCCGGGCGAATTGTGC 907 TS5-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGGCCCGTCGGGC 908 TS5-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCGCGGCTGT 909 TS5-83 TCCACGAGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 910 TS5-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 911 TS5-87 AGCGCCGCCGTGGCTCTGGACGCGGTCAACTATGCCGATA 912 TS5-88 CCCAATCCACAGGGGGTGGTTATCGGCATAGTTGACCGCG 913 GAV st-1 GAGAGGGGACAAGTTTGTACAAAAAAGCAGGCT 914 GAV st-2 GCAGTCGACAGGACGTGCATAGCCTGLTTTTTTGTACAAA 915 GAV st-3 ATGCACGTCCTGTCGACTGCGGTGCTGCTCGGCTCCGTTG 916 GAV st-4 TCCCAGGACCTTTTGAACGGCAACGGAGCCGAGCAGCACC 917 GAV st-5 CCGTTCAAAAGGTCCTGGGAAGACCAGGATCAAGCGGTCT 918 GAV st-6 ACCTCTTGGTGACGTCGGACAGACCGCTTGATCCTGGTCT 919 GAV st-7 GTCCGACGTCACCAAGAGGTCTGTTGACGACTTCATCAGC 920 GAV st-8 AGTGCAATAGGCGTCTCGGTGCTGATGAAGTCGTCAACAG 921 GAV st-9 ACCGAGACGCCTATTGCACTGAACAATCTTCTTTGCAATG 922 GAV st-10 ACGGCATCCATCAGGACCAACATTGCAAAGAAGATTGTTC 923 GAV st-11 TTGGTCCTGATGGATGCCGTGCATTCGGCACATCAGCTGG 924 GAV st-12 TGGGAGATGCAATCACCGCACCAGCTGATGTGCCGAATGC 925 GAV st-13 TGCGGTGATTGCATCTCCCAGCACACAAGACCCGGACTAC 926 GAV st-14 TCTCGCGTCCACATGTAATAGTAGTCCGGGTCTTGTGTGC 927 GAV st-15 TATTACATGTGGACGCGAGATAGCGCTCTTGTCTTCAAGA 928 GAV st-16 GGTGAAGCGGTCGATGAGGTTCTTGAAGACAAGAGCGCTA 929 GAV st-17 ACCTCATCGACCGCTTCACCGAAACGTACGATGCGGGCCT 930 GAV st-18 ACTGCTCGATGCGGCGCTGCAGGCCCGCATCGTACGTTTC 931 GAV st-19 GCAGCGCCGCATCGAGCAGTACATTACTGCCCAGGTCACT 932 GAV st-20 GGGTTAGAGAGGCCCTGGAGAGTGACCTGGGCAGTAATGT 933 GAV st-21 CTCCAGGGCCTCTCTAACCCCTCGGGCTCCCTCGCGGACG 934 GAV st-22 GGGCTCGCCGAGACCAGAGCCGTCCGCGAGGGAGCCCGAG 935 GAV st-23 GCTCTGGTCTCGGCGAGCCCAAGTTTGAGTTGACCCTGAA 936 GAV st-24 CCCAGTTGCCGGTGAAAGGCTTCAGGGTCAACTCAAACTT 937 GAV st-25 GCCTTTCACCGGCAACTGGGGTCGACCGCAGCGGGATGGC 938 GAV st-26 GCAATGGCTCGCAGAGCTGGGCCATCCCGCTGCGGTCGAC 939 GAV st-27 CCAGCTCTGCGAGCCATTGCCTTGATTGGATACTCAAAGT 940 GAV st-28 ATAGTTGTTGTTGATGAGCCACTTTGAGTATCCAATCAAG 941 GAV st-29 GGCTCATCAACAACAACTATCAGTCGACTGTGTCCAACGT 942 GAV st-30 TGCGCACAATAGGCCAGATGACGTTGGACACAGTCGACTG 943 GAV st-31 CATCTGGCCTATTGTGCGCAACGACCTCAACTATGTTGCC 944 GAV st-32 CCGGTTTGGTTCCAGTACTGGGCAACATAGTTGAGGTCGT 945 GAV st-33 CAGTACTGGAACCAAACCGGCTTTGACCTCTGGGAAGAAG 946 GAV st-34 AAAGAATGAGCTCCCATTGACTTCTTCCCAGAGGTCAAAG 947 GAV st-35 TCAATGGGAGCTCATTCTTTACTGTTGCCAACCAGCACCG 948 GAV st-36 TGGCGCCCTCGACAAGTGCTCGGTGCTGGTTGGCAACAGT 949 GAV st-37 AGCACTTGTCGAGGGCGCCACTCTTGCTGCCACTCTTGGC 950 GAV st-38 GAATAAGCGCTTCCCGACTGGCCAAGAGTGGCAGCAAGAG 951 GAV st-39 CAGTCGGGAAGCGCTTATTCATCTGTTGCTCCCCAGGTTT 952 GAV st-40 GAATCGTTGGAGAAAGCACAAAACCTGGGGAGCAACAGAT 953 GAV st-41 TGTGCTTTCTCCAACGATTCTGGGTGTCGTCTGGTGGATA 954 GAV st-42 TGTTGATGTTGGAGTCGACGTATCCACCAGACGACACCCA 955 GAV st-43 CGTCGACTCCAACATCAACACCAACGAGGGCAGGACTGGC 956 GAV st-44 AGGACGGAGTTGACATCCTTGCCAGTCCTGCCCTCGTTGG 957 GAV st-45 AAGGATGTCAACTCCGTCCTGACTTCCATCCACACCTTCG 958 GAV st-46 GTCACAGCCAAGGTTGGGATCGAAGGTGTGGATGGAAGTC 959 GAV st-47 ATCCCAACCTTGGCTGTGACGCAGGCACCTTCCAGCCATG 960 GAV st-48 TGGAGAGCGCTTTGTCACTGCATGGCTGGAAGGTGCCTGC 961 GAV st-49 CAGTGACAAAGCGCTCTCCAACCTCAAGGTTGTTGTCGAC 962 GAV st-50 CCGTAGATGGAGCGGAAGGAGTCGACAACAACCTTGAGGT 963 GAV st-51 TCCTTCCGCTCCATCTACGGCGTGAACAAGGGCATTCCTG 964 GAV st-52 AATGGCGACGGCAGCACCGGCAGGAATGCCCTTGTTCACG 965 GAV st-53 CCGGTGCTGCCGTCGCCATTGGCCGGTATGCAGAGGATGT 966 GAV st-54 AAGGGTTGCCGTTGTAGTACACATCCTCTGCATACCGGCC 967 GAV st-55 GTACTACAACGGCAACCCTTGGTATCTTGCTACATTTGCT 968 GAV st-56 TCGTACAGCTGCTCGGCAGCAGCAAATGTAGCAAGATACC 969 GAV st-57 GCTGCCGAGCAGCTGTACGATGCCATCTACGTCTGGAAGA 970 GAV st-58 CACCGTGATGGAGCCCGTCTTCTTCCAGACGTAGATGGCA 971 GAV st-59 AGACGGGCTCCATCACGGTGACCGCCACCTCCCTGGCCTT 972 GAV st-60 CAGGAACAAGCTCCTGGAAGAAGGCCAGGGAGGTGGCGGT 973 GAV st-61 CTTCCAGGAGCTTGTTCCTGGCGTGACGGCCGGGACCTAC 974 GAV st-62 AAGGTCGAAGAGCTGCTGGAGTAGGTCCCGGCCGTCACGC 975 GAV st-63 TCCAGCAGCTCTTCGACCTTTACCAACATCATCAACGCCG 976 GAV st-64 GCCATCGGCGTATGTCGAGACGGCGTTGATGATGTTGGTA 977 GAV st-65 TCTCGACATACGCCGATGGCTTCCTCAGCGAGGCTGCCAA 978 GAV st-66 AACCGTCGGCGGGGACGTACTTGGCAGCCTCGCTGAGGAA 979 GAV st-67 GTACGTCCCCGCCGACGGTTCGCTGGCCGAGCAGTTTGAC 980 GAV st-68 AGCGGAGTGCCGCTGTTGCGGTCAAACTGCTCGGCCAGCG 981 GAV st-69 CGCAACAGCGGCACTCCGCTGTCTGCGCTTCACCTGACGT 982 GAV st-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAAGCGCAGAC 983 GAV st-71 GGTCGTACGCCTCGTTCTTGACAGCCACGGCCCGTCGGGC 984 GAV st-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCGTGGCTGT 985 GAV st-73 TGGCATCGTGCCCCCCTCGTGGGCCAACAGCAGCGCTAGC 986 GAV st-74 GAGCACGTCGAGGGGATCGTGCTAGCGCTGCTGTTGGCCC 987 GAV st-75 ACGATCCCCTCGACGTGCTCCGGCGCGTCCGTGGTCGGAT 988 GAV st-76 GGCGGTGGGACGCGAGTAGGATCCGACCACGGACGCGCCG 989 GAV st-77 CCTACTCGCGTCCCACCGCCACGTCATTCCCTCCGTCGCA 990 GAV st-78 GCACGCCAGGCTTGGGCGTCTGCGACGGAGGGAATGACGT 991 GAV st-79 GACGCCCAAGCCTGGCGTGCCTTCCGGTACTCCCTACACG 992 GAV st-80 GGGGTCGCGCAGGGCAGGGGCGTGTAGGGAGTACCGGAAG 993 GAV st-81 CCCCTGCCCTGCGCGACCCCAACCTCCGTGGCCGTCACCT 994 GAV st-82 TGTCGACACGAGCTCGTGGAAGGTGACGGCCACGGAGGTT 995 GAV st-83 TCCACGAGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 996 GAV st-84 CCGCGGCGTTGCCCGCCACCTTGACCGTGTGGCCAAACTG 997 GAV st-85 GGTGGCGGGCAACGCCGCGGCCCTGGGCAACTGGAGCACG 998 GAV st-86 TCCAGAGCCACGGCGGCGCTCGTGCTCCAGTTGCCCAGGG 999 GAV st-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATGCCGATA 1000 GAV st-88 CCCAATCCACAGGGGGTGGTTATCGGCATAGTTGACGGCG 1001 GAV st-89 ACCACCCCCTGTGGATTGGGACGGTCAACCTCGAGGCTGG 1002 GAV st-90 ACTTGTACTCCACGACGTCTCCAGCCTCGAGGTTGACCGT 1003 GAV st-91 AGACGTCGTGGAGTACAAGTACATCAATGTGGGCCAAGAT 1004 GAV st-92 CTCTCCCAGGTCACGGAGCCATCTTGGCCCACATTGATGT 1005 GAV st-93 GGCTCCGTGACCTGGGAGAGTGATCCCAACCACACTTACA 1006 GAV st-94 ACAAGCCACCGCAGGAACCGTGTAAGTGTGGTTGGGATCA 1007 GAV st-95 CGGTTCCTGCGGTGGCTTGTGTGACGCAGGTTGTCAAGGA 1008 GAV st-96 TTTACGACTGCCAGGTGTCCTCCTTGACAACCTGCGTCAC 1009 GAV st-97 GGACACCTGGCAGTCGTAAACCCAGCTTTCTTGTACAAAG 1010 GAV st-98 CTCTGGGGACCACTTTGTACAAGAAAGCTGGG 1011 RB1-16 GGTGAAGCGGTCGATGAGGATCTTGAAGACAAGAGCGCTA 1012 RB1-17 TCCTCATCGACCGCTTCACCGAAACGTACGATGCGGGCCT 1013 RB1-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGGCCCGTCGGGC 1014 RB1-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCGCGGCTGT 1015 RB2-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 1016 RB2-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 1017 RB2-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGGCCCGTCGGGC 1018 RB2-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCGCGGCTGT 1019 RB3-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGCTCCGTCGGGC 1020 RB3-72 ACGAGGGGGGCACGATGCCAGCCCGACGGAGCGCGGCTGT 1021 RB1-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGGCCCGTCGGGC 1022 RB1-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCGCGGCTGT 1023 RB4-82 TGTCGACACGAGCGCGTGGAAGGTGACGGCCACGGAGGTT 1024 RB4-83 TCCACGCGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 1025 RB4-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGGCCCGTCGGGC 1026 RB4-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCGCGGCTGT 1027 RB5-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGGCCCGTCGGGC 1028 RB5-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCGCGGCTGT 1029 RB5-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATCGCGATA 1030 RB5-88 CCCAATCCACAGGGGGTGGTTATCGCGATAGTTGACGGCG 1031 RB6-16 GGTGAAGCGGTCGATGAGGATCTTGAAGACAAGAGCGCTA 1032 RB6-17 TCCTCATCGACCGCTTCACCGAAACGTACGATGCGGGCCT 1033 RB6-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGGCCCGTCGGGC 1034 RB6-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCGCGGCTGT 1035 RB6-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATCGCGATA 1036 RB6-88 CCCAATCCACAGGGGGTGGTTATCGCGATAGTTGACGGCG 1037 RB7-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 1038 RB7-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 1039 RB7-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGGCCCGTCGGGC 1040 RB7-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCGCGGCTGT 1041 RB7-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATCGCGATA 1042 RB7-88 CCCAATCCACAGGGGGTGGTTATCGCGATAGTTGACGGCG 1043 RB8-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGCTCCGTCGGGC 1044 RB8-72 ACGAGGGGGGCACGATGCCAGCCCGACGGAGCGCGGCTGT 1045 RB8-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATCGCGATA 1046 RB8-88 CCCAATCCACAGGGGGTGGTTATCGCGATAGTTGACGGCG 1047 RB9-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGCTCCGTCGGGC 1048 RB9-72 ACGAGGGGGGCACGATGCCAGCCCGACGGAGCGCGGCTGT 1049 RB9-82 TGTCGACACGAGCGCGTGGAAGGTGACGGCCACGGAGGTT 1050 RB9-83 TCCACGCGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 1051 RB10-16 GGTGAAGCGGTCGATGAGGATCTTGAAGACAAGAGCGCTA 1052 RB10-17 TCCTCATCGACCGCTTCACCGAAACGTACGATGCGGGCCT 1053 RB10-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGCTCCGTCGGGC 1054 RB10-72 ACGAGGGGGGCACGATGCCAGCCCGACGGAGCGCGGCTGT 1055 RB10-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATCGCGATA 1056 RB10-88 CCCAATCCACAGGGGGTGGTTATCGCGATAGTTGACGGCG 1057 RB11-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 1058 RB11-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 1059 RB11-71 GGTCGTACGCCTCGTTCTTGACAGCCGCGCTCCGTCGGGC 1060 RB11-72 ACGAGGGGGGCACGATGCCAGCCCGACGGAGCGCGGCTGT 1061 RB11-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATCGCGATA 1062 RB11-88 CCCAATCCACAGGGGGTGGTTATCGCGATAGTTGACGGCG 1063 RB12-16 GGTGAAGCGGTCGATGAGGATCTTGAAGACAAGAGCGCTA 1064 RB12-17 TCCTCATCGACCGCTTCACCGAAACGTACGATGCGGGCCT 1065 RB13-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 1066 RB13-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 1067 RB14-71 GGTCGTACGCCTCGTTCTTGACAGCCACGCTCCGTCGGGC 1068 RB14-72 ACGAGGGGGGCACGATGCCAGCCCGACGGAGCGTGGCTGT 1069 RB15-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATCGCGATA 1070 RB15-88 CCCAATCCACAGGGGGTGGTTATCGCGATAGTTGACGGCG 1071 RB16-16 GGTGAAGCGGTCGATGAGGATCTTGAAGACAAGAGCGCTA 1072 RB16-17 TCCTCATCGACCGCTTCACCGAAACGTACGATGCGGGCCT 1073 RB16-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATCGCGATA 1074 RB16-88 CCCAATCCACAGGGGGTGGTTATCGCGATAGTTGACGGCG 1075 RB17-82 TGTCGACACGAGCGCGTGGAAGGTGACGGCCACGGAGGTT 1076 RB17-83 TCCACGCGCTCGTGTCGACACAGTTTGGCCACACGGTCAA 1077 RB17-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATCGCGATA 1078 RB17-88 CCCAATCCACAGGGGGTGGTTATCGCGATAGTTGACGGCG 1079 RB18-71 GGTCGTACGCCTCGTTCTTGACAGCCATGGCCCGTCGGGC 1080 RB18-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCATGGCTGT 1081 RB18-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATCGCGATA 1082 RB18-88 CCCAATCCACAGGGGGTGGTTATCGCGATAGTTGACGGCG 1083 RB19-16 GGTGAAGCGGTCGATGAGGATCTTGAAGACAAGAGCGCTA 1084 RB19-17 TCCTCATCGACCGCTTCACCGAAACGTACGATGCGGGCCT 1085 RB19-71 GGTCGTACGCCTCGTTCTTGACAGCCATGGCCCGTCGGGC 1086 RB19-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCATGGCTGT 1087 RB19-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATCGCGATA 1088 RB19-88 CCCAATCCACAGGGGGTGGTTATCGCGATAGTTGACGGCG 1089 RB20-16 GGTGAAGCGGTCGATGAGGATCTTGAAGACAAGAGCGCTA 1090 RB20-17 TCCTCATCGACCGCTTCACCGAAACGTACGATGCGGGCCT 1091 RB20-69 CGCAACAGCGGCACTCCGCTGTCTGCGGTTCACCTGACGT 1092 RB20-70 CAAGAACGAGGCGTACGACCACGTCAGGTGAACCGCAGAC 1093 RB20-71 GGTCGTACGCCTCGTTCTTGACAGCCATGGCCCGTCGGGC 1094 RB20-72 ACGAGGGGGGCACGATGCCAGCCCGACGGGCCATGGCTGT 1095 RB20-87 AGCGCCGCCGTGGCTCTGGACGCCGTCAACTATCGCGATA 1096 RB20-88 CCCAATCCACAGGGGGTGGTTATCGCGATAGTTGACGGCG 1097 PIs of representative combinatorial variants Variant Mutations DP2 DP3 DP4 DP5 DP6 DP7 CS Ts Liq. ALL1 I43Q/D44C/L417V/E503A/Q511H/A539R 0.89 1.22 1.08 1.10 1.17 1.02 1.27 1.95 1.59 ALL2 I43Q/L417V/E503A/Q511H/A539R 1.13 1.50 1.24 1.19 1.32 1.24 1.52 1.84 1.96 ALL3 I43Q/D44C/N61I/L417V/E503A/Q511H/ 0.69 1.09 0.91 0.89 0.96 0.99 1.30 1.43 1.64 A539R ALL4 I43Q/N61I/L417V/E503A/Q511H/A539R 0.89 1.40 1.15 1.15 1.25 1.12 1.52 1.79 1.73 ALL5 I43R/L417V/E503A/Q511H/A539R 1.10 1.50 N/D N/D N/D 1.04 1.17 2.37 1.87 ALL6 I43R/N61I/L417V/E503A/Q511H/A539R 0.93 1.52 N/D N/D N/D 1.37 1.53 1.84 2.24 ALL7 I43R/L417R/E503A/A539R 1.19 1.38 1.29 1.23 1.33 1.20 1.54 1.67 1.62 ALL8 I43R/N61I/L417R/E503A/Q511H/A539R 1.07 1.56 N/D N/D N/D 1.08 1.14 1.84 2.11 C1 G73F/T430A/Q511H 0.82 0.80 0.95 0.95 1.06 0.94 1.07 1.84 0.96 C2 I43R/G73F/T430A 0.96 0.97 1.14 1.17 1.28 1.07 1.25 1.91 1.18 C4 G73F/T430A/E503V/Q511H 0.97 0.80 1.10 1.08 1.17 1.04 1.06 2.57 1.01 C5 D44C/G73F/N563K 0.77 0.77 0.86 0.87 0.95 0.77 0.71 2.16 0.97 C7 D44C/G73F/E503V/Q511H 0.74 0.71 0.82 0.84 0.93 0.78 0.79 2.10 0.89 C8 D44C/G73F/N563K 0.78 0.76 0.81 0.91 0.94 0.79 1.05 2.28 N/D C9 D44C/G73F/L417R/N563K 0.82 0.86 0.96 1.07 1.08 0.96 1.00 2.57 1.22 C11 D44C/G73F/N563K 0.74 0.68 0.81 0.92 0.90 0.76 1.04 2.42 N/D C12 I43R/T430A 1.02 1.06 1.21 1.21 1.32 1.03 1.35 1.60 1.26 C13 I43Q/T430A 0.96 0.94 1.13 1.14 1.24 1.04 1.29 1.10 1.45 C14 I43Q/T430A/Q511H 1.08 1.11 1.13 1.14 1.23 1.13 1.34 1.33 1.46 C15 D44C/L417R/N563K 0.84 0.88 0.95 1.07 1.08 0.85 1.09 2.30 0.99 CS1 L417V/T430A/A431L/Q511H/A535R/ 0.78 1.19 1.35 1.29 1.42 1.28 1.44 1.56 2.35 A539R/N563I CS2 L417V/T430A/A431Q/Q511H/A535R/ 0.96 1.39 1.46 1.42 1.52 1.60 1.77 1.56 2.32 A539R/N563I CS3 L417V/T430A/Q511H/A535R/N563I 1.00 1.17 N/D N/D N/D 0.98 1.40 1.69 1.78 CS4 L417V/T430A/Q511H/A539R/N563I 1.11 1.36 N/D N/D N/D 1.21 1.53 1.95 1.73 LQ1 G294C/L417R/A431L 1.10 1.47 1.18 1.18 1.35 1.10 0.98 1.04 1.77 LQ2 G294C/L417V/A431Q 1.15 1.56 1.32 1.30 1.46 1.22 1.08 1.02 2.08 LQ3 G294C/L417V/A431L/Q511H 0.99 1.41 N/D N/D N/D N/D 1.21 1.29 2.07 LQ4 G294C/L417R/A431Q/Q511H 1.20 1.49 1.11 1.13 1.27 1.08 1.19 1.43 1.65 LQ5 L417R/A431L/Q511H N/D N/D N/D N/D N/D 1.02 1.21 1.56 1.88 LQ6 L417V/A431Q/Q511H 0.94 1.30 1.20 1.18 1.28 1.25 1.33 1.35 2.05 RB1 I43Q/T430A/Q511H/N61I 0.90 1.13 1.00 1.03 1.13 1.08 1.15 1.27 1.47 RB2 I43Q/T430A/Q511H/L417V 1.12 1.34 N/D N/D N/D 1.09 1.38 1.42 1.87 RB3 I43Q/T430A/Q511H/A431L 0.87 1.05 1.03 1.05 1.15 1.10 1.25 1.29 1.70 RB4 I43Q/T430A/Q511H/E503A 0.99 1.00 1.05 1.04 1.13 1.09 1.29 1.47 1.50 RB5 I43Q/T430A/Q511H/A539R 0.98 1.22 1.06 1.02 1.11 1.10 1.45 1.47 1.59 RB6 I43Q/T430A/Q511H/N61I/A539R 0.75 1.09 1.09 1.05 1.14 1.23 N/D 0.94 N/D RB7 I43Q/T430A/Q511H/L417V/A539R 1.20 1.62 N/D N/D N/D 1.29 1.44 1.85 2.17 RB8 I43Q/T430A/Q511H/A431L/A539R 0.90 1.38 N/D N/D N/D 1.25 1.38 1.59 2.18 RB9 I43Q/T430A/Q511H/A431L/E503A 0.79 0.82 0.95 0.92 1.02 1.03 1.39 1.69 1.55 RB10 I43Q/T430A/Q511H/N61I/A539R/A431L 0.68 1.27 N/D N/D N/D 0.87 1.47 1.29 1.73 RB11 I43Q/T430A/Q511H/L417V/A539R/A431L 0.89 1.50 N/D N/D N/D 1.05 1.36 1.58 2.03 RB12 I43Q/Q511H/N61I 0.75 0.80 0.91 0.91 1.00 0.82 1.25 1.37 1.56 RB13 I43Q/Q511H/L417V 0.97 0.94 0.96 0.93 1.05 0.94 1.38 1.50 1.50 RB14 I43Q/Q511H/A431L 0.73 0.75 0.89 0.88 0.94 0.89 1.31 1.37 1.55 RB15 I43Q/Q511H/A539R 0.90 0.88 1.03 0.99 1.07 1.05 1.42 1.52 1.69 RB16 I43Q/Q511H/A539R/N61I 0.78 0.96 1.22 1.18 1.26 0.94 1.43 1.60 1.34 RB17 I43Q/Q511H/A539R/E503A 1.02 1.15 1.16 1.12 1.21 1.20 1.38 1.68 1.40 RB18 I43Q/Q511H/A539R/T430M 0.81 0.84 1.03 0.99 1.08 0.54 1.44 1.64 1.40 RB19 I43Q/Q511H/A539R/T430M/N61I 0.77 1.21 N/D N/D N/D 1.07 1.50 1.47 1.88 RB20 I43Q/Q511H/A539R/T430M/N61I/L417V 0.73 1.35 N/D N/D N/D 0.96 1.55 1.79 1.95 TS1 I43R/T430A/E503V/A535R/N563K 1.09 0.95 1.13 1.09 1.17 1.19 N/D 2.13 N/D TS2 D44R/E503A/Q511H/N563I 0.80 0.70 0.88 0.89 0.96 0.85 1.14 1.53 1.23 TS3 E503A/N563I 0.93 0.73 0.91 0.88 0.96 0.92 1.17 1.39 1.04 TS4 I43R/T430A/E503A/Q511H/N563K 0.92 0.77 0.95 0.89 1.02 1.06 1.33 1.66 1.33 TS5 D44R/T430A/Q511H/A535R 0.74 0.68 0.83 0.83 0.91 0.91 0.95 1.59 1.21 Var1 L417V/A431L/A539R 0.69 1.06 N/D 1.12 N/D 1.16 1.26 1.18 1.40 Var2 L417V/A431L/A539R/I43Q 0.69 1.13 N/D 1.15 N/D 1.18 1.40 1.12 1.53 Var3 L417V/A431L/A539R/N61I 0.43 0.91 N/D 0.99 N/D 1.06 1.29 1.14 1.38 Var4 L417V/A431L/A539R/A535R 0.64 0.97 N/D 1.03 N/D 1.07 1.22 1.49 1.22 Var5 L417V/A431L/A539R/I43Q/N61I 0.38 0.86 N/D 0.94 N/D 1.04 1.25 1.07 1.24 Var6 L417V/A431L/A539R/N61I/A535R 0.32 0.72 N/D 0.82 N/D 0.90 1.16 1.86 1.15 Var7 L417V/A431L/A539R/A535R/I43Q 0.65 0.99 N/D 1.03 N/D 1.10 1.22 1.29 1.26 Var8 L417V/A431L/A539R/I43Q/N61I/A535R 0.32 0.73 N/D 0.80 N/D 0.94 1.11 1.08 1.12 Var9 L417V/A431L/A539R/143Q/N61I/ 0.25 0.70 N/D 0.71 N/D 0.84 0.99 1.13 1.14 A535R/T430A Var10 L417V/T430A/A431L/Q511H/A535R/ 0.53 0.98 N/D 0.97 N/D 1.06 1.08 1.86 1.63 A539R/N563I/I43Q Var11 L417V/T430A/A431L/Q511H/A535R/ 0.38 0.80 N/D 0.86 N/D 0.95 1.16 1.51 1.15 A539R/N563I/N61I Var12 L417V/T430A/A431L/Q511H/A535R/ 0.31 0.78 N/D 0.84 N/D 0.94 1.17 1.81 1.30 A539R/N563I/I43Q/N61I Var13 L417V/A431L/A539R/I43R 0.67 1.08 N/D 1.12 N/D 1.18 1.32 1.83 1.55 Var14 L417V/A431L/A539R/I43R/N61I 0.43 0.99 N/D 1.01 N/D 1.09 1.24 1.70 1.48 Var15 L417V/A431L/A539R/I43R/N61I/ 0.39 0.94 N/D 0.96 N/D 1.09 1.34 1.96 1.59 A535R/T430A Var16 L417R/A431L/A539R 0.70 1.01 N/D 1.03 N/D 1.11 1.23 1.33 1.31 Var17 L417G/A431L/A539R 0.70 1.15 N/D 1.14 N/D 1.19 1.20 1.23 1.42 Var18 G73F/E503V/N563K/L417R/A539R 0.93 1.14 N/D 1.12 N/D 1.11 1.08 2.71 0.98 Var19 G73F/E503V/N563K/I43R/L417R/A539R 1.24 1.47 N/D 1.43 N/D 1.33 1.38 2.58 1.21 Var20 G73F/E503V/N563K/I43R/Q511H 0.94 0.95 N/D 0.95 N/D 0.97 1.02 2.47 0.84 Example 9
Homology Between TrGA and AaGA
Example 10
Model of Acarbose Binding to TrGA
Example 11
Enzymes Used
Results:
Glucoamylase α-Amylase Pullulanase added added added RDF mg GAU/ SSU/ g prod./ PU/ g. prod./ Enzyme Protein kg kg kg kg kg Average Dose composition /kg grist grist grist grist grist grist (n = 3) StDev 1 DiazymeX4 1022 2871 1768* — 83.3 0.047 2 TrGA 1022 4088 82.3 0.054 3 BRW1 1022 3781 83.2 0.050 4 BRW1 2044 7563 84.8 0.001 5 BRW1 + 1022 3781 28172 2.46 1961 2.06 84.1 0.098 GC626 + Diazyme P10 6 BRW1 + 2044 7563 56344 4.93 3907 4.11 85.1 0.169 GC626 + Diazyme P10 Sequences
SEQ ID NO: 1: <210> 1 <211> 632 <212> PRT <213> <400> 1 Met His Val Leu Ser Thr Ala Val Leu Leu Gly Ser Val Ala Val Gln 1 5 10 15 Lys Val Leu Gly Arg Pro Gly Ser Ser Gly Leu Ser Asp Val Thr Lys 20 25 30 Arg Ser Val Asp Asp Phe Ile Ser Thr Glu Thr Pro Ile Ala Leu Asn 35 40 45 Asn Leu Leu Cys Asn Val Gly Pro Asp Gly Cys Arg Ala Phe Gly Thr 50 55 60 Ser Ala Gly Ala Val Ile Ala Ser Pro Ser Thr Ile Asp Pro Asp Tyr 65 70 75 80 Tyr Tyr Met Trp Thr Arg Asp Ser Ala Leu Val Phe Lys Asn Leu Ile 85 90 95 Asp Arg Phe Thr Glu Thr Tyr Asp Ala Gly Leu Gln Arg Arg Ile Glu 100 105 110 Gln Tyr Ile Thr Ala Gln Val Thr Leu Gln Gly Leu Ser Asn Pro Ser 115 120 125 Gly Ser Leu Ala Asp Gly Ser Gly Leu Gly Glu Pro Lys Phe Glu Leu 130 135 140 Thr Leu Lys Pro Phe Thr Gly Asn Trp Gly Arg Pro Gln Arg Asp Gly 145 150 155 160 Pro Ala Leu Arg Ala Ile Ala Leu Ile Gly Tyr Ser Lys Trp Leu Ile 165 170 175 Asn Asn Asn Tyr Gln Ser Thr Val Ser Asn Val Ile Trp Pro Ile Val 180 185 190 Arg Asn Asp Leu Asn Tyr Val Ala Gln Tyr Trp Asn Gln Thr Gly Phe 195 200 205 Asp Leu Trp Glu Glu Val Asn Gly Ser Ser Phe Phe Thr Val Ala Asn 210 215 220 Gln His Arg Ala Leu Val Glu Gly Ala Thr Leu Ala Ala Thr Leu Gly 225 230 235 240 Gln Ser Gly Ser Ala Tyr Ser Ser Val Ala Pro Gln Val Leu Cys Phe 245 250 255 Leu Gln Arg Phe Trp Val Ser Ser Gly Gly Tyr Val Asp Ser Asn Ile 260 265 270 Asn Thr Asn Glu Gly Arg Thr Gly Lys Asp Val Asn Ser Val Leu Thr 275 280 285 Ser Ile His Thr Phe Asp Pro Asn Leu Gly Cys Asp Ala Gly Thr Phe 290 295 300 Gln Pro Cys Ser Asp Lys Ala Leu Ser Asn Leu Lys Val Val Val Asp 305 310 315 320 Ser Phe Arg Ser Ile Tyr Gly Val Asn Lys Gly Ile Pro Ala Gly Ala 325 330 335 Ala Val Ala Ile Gly Arg Tyr Ala Glu Asp Val Tyr Tyr Asn Gly Asn 340 345 350 Pro Trp Tyr Leu Ala Thr Phe Ala Ala Ala Glu Gln Leu Tyr Asp Ala 355 360 365 Ile Tyr Val Trp Lys Lys Thr Gly Ser Ile Thr Val Thr Ala Thr Ser 370 375 380 Leu Ala Phe Phe Gln Glu Leu Val Pro Gly Val Thr Ala Gly Thr Tyr 385 390 395 400 Ser Ser Ser Ser Ser Thr Phe Thr Asn Ile Ile Asn Ala Val Ser Thr 405 410 415 Tyr Ala Asp Gly Phe Leu Ser Glu Ala Ala Lys Tyr Val Pro Ala Asp 420 425 430 Gly Ser Leu Ala Glu Gln Phe Asp Arg Asn Ser Gly Thr Pro Leu Ser 435 440 445 Ala Leu His Leu Thr Trp Ser Tyr Ala Ser Phe Leu Thr Ala Thr Ala 450 455 460 Arg Arg Ala Gly Ile Val Pro Pro Ser Trp Ala Asn Ser Ser Ala Ser 465 470 475 480 Thr Ile Pro Ser Thr Cys Ser Gly Ala Ser Val Val Gly Ser Tyr Ser 485 490 495 Arg Pro Thr Ala Thr Ser Phe Pro Pro Ser Gln Thr Pro Lys Pro Gly 500 505 510 Val Pro Ser Gly Thr Pro Tyr Thr Pro Leu Pro Cys Ala Thr Pro Thr 515 520 525 Ser Val Ala Val Thr Phe His Glu Leu Val Ser Thr Gln Phe Gly Gln 530 535 540 Thr Val Lys Val Ala Gly Asn Ala Ala Ala Leu Gly Asn Trp Ser Thr 545 550 555 560 Ser Ala Ala Val Ala Leu Asp Ala Val Asn Tyr Ala Asp Asn His Pro 565 570 575 Leu Trp Ile Gly Thr Val Asn Leu Glu Ala Gly Asp Val Val Glu Tyr 580 585 590 Lys Tyr Ile Asn Val Gly Gln Asp Gly Ser Val Thr Trp Glu Ser Asp 595 600 605 Pro Asn His Thr Tyr Thr Val Pro Ala Val Ala Cys Val Thr Gln Val 610 615 620 Val Lys Glu Asp Thr Trp Gln Ser 625 630 SEQ ID NO: 2: peptide <210> 2 <211> 599 <212> PRT <213> <400> 2 Ser Val Asp Asp Phe Ile Ser Thr Glu Thr Pro Ile Ala Leu Asn Asn 1 5 10 15 Leu Leu Cys Asn Val Gly Pro Asp Gly Cys Arg Ala Phe Gly Thr Ser 20 25 30 Ala Gly Ala Val Ile Ala Ser Pro Ser Thr Ile Asp Pro Asp Tyr Tyr 35 40 45 Tyr Met Trp Thr Arg Asp Ser Ala Leu Val Phe Lys Asn Leu Ile Asp 50 55 60 Arg Phe Thr Glu Thr Tyr Asp Ala Gly Leu Gln Arg Arg Ile Glu Gln 65 70 75 80 Tyr Ile Thr Ala Gln Val Thr Leu Gln Gly Leu Ser Asn Pro Ser Gly 85 90 95 Ser Leu Ala Asp Gly Ser Gly Leu Gly Glu Pro Lys Phe Glu Leu Thr 100 105 110 Leu Lys Pro Phe Thr Gly Asn Trp Gly Arg Pro Gln Arg Asp Gly Pro 115 120 125 Ala Leu Arg Ala Ile Ala Leu Ile Gly Tyr Ser Lys Trp Leu Ile Asn 130 135 140 Asn Asn Tyr Gln Ser Thr Val Ser Asn Val Ile Trp Pro Ile Val Arg 145 150 155 160 Asn Asp Leu Asn Tyr Val Ala Gln Tyr Trp Asn Gln Thr Gly Phe Asp 165 170 175 Leu Trp Glu Glu Val Asn Gly Ser Ser Phe Phe Thr Val Ala Asn Gln 180 185 190 His Arg Ala Leu Val Glu Gly Ala Thr Leu Ala Ala Thr Leu Gly Gln 195 200 205 Ser Gly Ser Ala Tyr Ser Ser Val Ala Pro Gln Val Leu Cys Phe Leu 210 215 220 Gln Arg Phe Trp Val Ser Ser Gly Gly Tyr Val Asp Ser Asn Ile Asn 225 230 235 240 Thr Asn Glu Gly Arg Thr Gly Lys Asp Val Asn Ser Val Leu Thr Ser 245 250 255 Ile His Thr Phe Asp Pro Asn Leu Gly Cys Asp Ala Gly Thr Phe Gln 260 265 270 Pro Cys Ser Asp Lys Ala Leu Ser Asn Leu Lys Val Val Val Asp Ser 275 280 285 Phe Arg Ser Ile Tyr Gly Val Asn Lys Gly Ile Pro Ala Gly Ala Ala 290 295 300 Val Ala Ile Gly Arg Tyr Ala Glu Asp Val Tyr Tyr Asn Gly Asn Pro 305 310 315 320 Trp Tyr Leu Ala Thr Phe Ala Ala Ala Glu Gln Leu Tyr Asp Ala Ile 325 330 335 Tyr Val Trp Lys Lys Thr Gly Ser Ile Thr Val Thr Ala Thr Ser Leu 340 345 350 Ala Phe Phe Gln Glu Leu Val Pro Gly Val Thr Ala Gly Thr Tyr Ser 355 360 365 Ser Ser Ser Ser Thr Phe Thr Asn Ile Ile Asn Ala Val Ser Thr Tyr 370 375 380 Ala Asp Gly Phe Leu Ser Glu Ala Ala Lys Tyr Val Pro Ala Asp Gly 385 390 395 400 Ser Leu Ala Glu Gln Phe Asp Arg Asn Ser Gly Thr Pro Leu Ser Ala 405 410 415 Leu His Leu Thr Trp Ser Tyr Ala Ser Phe Leu Thr Ala Thr Ala Arg 420 425 430 Arg Ala Gly Ile Val Pro Pro Ser Trp Ala Asn Ser Ser Ala Ser Thr 435 440 445 Ile Pro Ser Thr Cys Ser Gly Ala Ser Val Val Gly Ser Tyr Ser Arg 450 455 460 Pro Thr Ala Thr Ser Phe Pro Pro Ser Gln Thr Pro Lys Pro Gly Val 465 470 475 480 Pro Ser Gly Thr Pro Tyr Thr Pro Leu Pro Cys Ala Thr Pro Thr Ser 485 490 495 Val Ala Val Thr Phe His Glu Leu Val Ser Thr Gln Phe Gly Gln Thr 500 505 510 Val Lys Val Ala Gly Asn Ala Ala Ala Leu Gly Asn Trp Ser Thr Ser 515 520 525 Ala Ala Val Ala Leu Asp Ala Val Asn Tyr Ala Asp Asn His Pro Leu 530 535 540 Trp Ile Gly Thr Val Asn Leu Glu Ala Gly Asp Val Val Glu Tyr Lys 545 550 555 560 Tyr Ile Asn Val Gly Gln Asp Gly Ser Val Thr Trp Glu Ser Asp Pro 565 570 575 Asn His Thr Tyr Thr Val Pro Ala Val Ala Cys Val Thr Gln Val Val 580 585 590 Lys Glu Asp Thr Trp Gln Ser 595 SEQ ID NO: 3: TrGA, CD <210> 3 <211> 453 <212> PRT <213> <400> 3 Ser Val Asp Asp Phe Ile Ser Thr Glu Thr Pro Ile Ala Leu Asn Asn 1 5 10 15 Leu Leu Cys Asn Val Gly Pro Asp Gly Cys Arg Ala Phe Gly Thr Ser 20 25 30 Ala Gly Ala Val Ile Ala Ser Pro Ser Thr Ile Asp Pro Asp Tyr Tyr 35 40 45 Tyr Met Trp Thr Arg Asp Ser Ala Leu Val Phe Lys Asn Leu Ile Asp 50 55 60 Arg Phe Thr Glu Thr Tyr Asp Ala Gly Leu Gln Arg Arg Ile Glu Gln 65 70 75 80 Tyr Ile Thr Ala Gln Val Thr Leu Gln Gly Leu Ser Asn Pro Ser Gly 85 90 95 Ser Leu Ala Asp Gly Ser Gly Leu Gly Glu Pro Lys Phe Glu Leu Thr 100 105 110 Leu Lys Pro Phe Thr Gly Asn Trp Gly Arg Pro Gln Arg Asp Gly Pro 115 120 125 Ala Leu Arg Ala Ile Ala Leu Ile Gly Tyr Ser Lys Trp Leu Ile Asn 130 135 140 Asn Asn Tyr Gln Ser Thr Val Ser Asn Val Ile Trp Pro Ile Val Arg 145 150 155 160 Asn Asp Leu Asn Tyr Val Ala Gln Tyr Trp Asn Gln Thr Gly Phe Asp 165 170 175 Leu Trp Glu Glu Val Asn Gly Ser Ser Phe Phe Thr Val Ala Asn Gln 180 185 190 His Arg Ala Leu Val Glu Gly Ala Thr Leu Ala Ala Thr Leu Gly Gln 195 200 205 Ser Gly Ser Ala Tyr Ser Ser Val Ala Pro Gln Val Leu Cys Phe Leu 210 215 220 Gln Arg Phe Trp Val Ser Ser Gly Gly Tyr Val Asp Ser Asn Ile Asn 225 230 235 240 Thr Asn Glu Gly Arg Thr Gly Lys Asp Val Asn Ser Val Leu Thr Ser 245 250 255 Ile His Thr Phe Asp Pro Asn Leu Gly Cys Asp Ala Gly Thr Phe Gln 260 265 270 Pro Cys Ser Asp Lys Ala Leu Ser Asn Leu Lys Val Val Val Asp Ser 275 280 285 Phe Arg Ser Ile Tyr Gly Val Asn Lys Gly Ile Pro Ala Gly Ala Ala 290 295 300 Val Ala Ile Gly Arg Tyr Ala Glu Asp Val Tyr Tyr Asn Gly Asn Pro 305 310 315 320 Trp Tyr Leu Ala Thr Phe Ala Ala Ala Glu Gln Leu Tyr Asp Ala Ile 325 330 335 Tyr Val Trp Lys Lys Thr Gly Ser Ile Thr Val Thr Ala Thr Ser Leu 340 345 350 Ala Phe Phe Gln Glu Leu Val Pro Gly Val Thr Ala Gly Thr Tyr Ser 355 360 365 Ser Ser Ser Ser Thr Phe Thr Asn Ile Ile Asn Ala Val Ser Thr Tyr 370 375 380 Ala Asp Gly Phe Leu Ser Glu Ala Ala Lys Tyr Val Pro Ala Asp Gly 385 390 395 400 Ser Leu Ala Glu Gln Phe Asp Arg Asn Ser Gly Thr Pro Leu Ser Ala 405 410 415 Leu His Leu Thr Trp Ser Tyr Ala Ser Phe Leu Thr Ala Thr Ala Arg 420 425 430 Arg Ala Gly Ile Val Pro Pro Ser Trp Ala Asn Ser Ser Ala Ser Thr 435 440 445 Ile Pro Ser Thr Cys 450 SEQ ID NO: 4: <210> 4 <211> 1899 <212> DNA <213> <400> 4 atgcacgtcc tgtcgactgc ggtgctgctc ggctccgttg ccgttcaaaa ggtcctggga 60 agaccaggat caagcggtct gtccgacgtc accaagaggt ctgttgacga cttcatcagc 120 accgagacgc ctattgcact gaacaatctt ctttgcaatg ttggtcctga tggatgccgt 180 gcattcggca catcagctgg tgcggtgatt gcatctccca gcacaattga cccggactac 240 tattacatgt ggacgcgaga tagcgctctt gtcttcaaga acctcatcga ccgcttcacc 300 gaaacgtacg atgcgggcct gcagcgccgc atcgagcagt acattactgc ccaggtcact 360 ctccagggcc tctctaaccc ctcgggctcc ctcgcggacg gctctggtct cggcgagccc 420 aagtttgagt tgaccctgaa gcctttcacc ggcaactggg gtcgaccgca gcgggatggc 480 ccagctctgc gagccattgc cttgattgga tactcaaagt ggctcatcaa caacaactat 540 cagtcgactg tgtccaacgt catctggcct attgtgcgca acgacctcaa ctatgttgcc 600 cagtactgga accaaaccgg ctttgacctc tgggaagaag tcaatgggag ctcattcttt 660 actgttgcca accagcaccg agcacttgtc gagggcgcca ctcttgctgc cactcttggc 720 cagtcgggaa gcgcttattc atctgttgct ccccaggttt tgtgctttct ccaacgattc 780 tgggtgtcgt ctggtggata cgtcgactcc aacatcaaca ccaacgaggg caggactggc 840 aaggatgtca actccgtcct gacttccatc cacaccttcg atcccaacct tggctgtgac 900 gcaggcacct tccagccatg cagtgacaaa gcgctctcca acctcaaggt tgttgtcgac 960 tccttccgct ccatctacgg cgtgaacaag ggcattcctg ccggtgctgc cgtcgccatt 1020 ggccggtatg cagaggatgt gtactacaac ggcaaccctt ggtatcttgc tacatttgct 1080 gctgccgagc agctgtacga tgccatctac gtctggaaga agacgggctc catcacggtg 1140 accgccacct ccctggcctt cttccaggag cttgttcctg gcgtgacggc cgggacctac 1200 tccagcagct cttcgacctt taccaacatc atcaacgccg tctcgacata cgccgatggc 1260 ttcctcagcg aggctgccaa gtacgtcccc gccgacggtt cgctggccga gcagtttgac 1320 cgcaacagcg gcactccgct gtctgcgctt cacctgacgt ggtcgtacgc ctcgttcttg 1380 acagccacgg cccgtcgggc tggcatcgtg cccccctcgt gggccaacag cagcgctagc 1440 acgatcccct cgacgtgctc cggcgcgtcc gtggtcggat cctactcgcg tcccaccgcc 1500 acgtcattcc ctccgtcgca gacgcccaag cctggcgtgc cttccggtac tccctacacg 1560 cccctgccct gcgcgacccc aacctccgtg gccgtcacct tccacgagct cgtgtcgaca 1620 cagtttggcc agacggtcaa ggtggcgggc aacgccgcgg ccctgggcaa ctggagcacg 1680 agcgccgccg tggctctgga cgccgtcaac tatgccgata accaccccct gtggattggg 1740 acggtcaacc tcgaggctgg agacgtcgtg gagtacaagt acatcaatgt gggccaagat 1800 ggctccgtga cctgggagag tgatcccaac cacacttaca cggttcctgc ggtggcttgt 1860 gtgacgcagg ttgtcaagga ggacacctgg cagtcgtaa 1899 SEQ ID NO: 5: <210> 5 <211> 448 <212> PRT <213> <400> 5 Ala Thr Leu Asp Ser Trp Leu Ser Asn Glu Ala Thr Val Ala Arg Thr 1 5 10 15 Ala Ile Leu Asn Asn Ile Gly Ala Asp Gly Ala Trp Val Ser Gly Ala 20 25 30 Asp Ser Gly Ile Val Val Ala Ser Pro Ser Thr Asp Asn Pro Asp Tyr 35 40 45 Phe Tyr Thr Trp Thr Arg Asp Ser Gly Leu Val Ile Lys Thr Leu Val 50 55 60 Asp Leu Phe Arg Asn Gly Asp Thr Asp Leu Leu Ser Thr Ile Glu Asn 65 70 75 80 Tyr Ile Ser Ser Gln Ala Ile Val Gln Gly Ile Ser Asn Pro Ser Gly 85 90 95 Asp Leu Ser Ser Gly Gly Leu Gly Glu Pro Lys Phe Asn Val Asp Glu 100 105 110 Thr Ala Tyr Thr Gly Ser Trp Gly Arg Pro Gln Arg Asp Gly Pro Ala 115 120 125 Leu Arg Ala Thr Ala Met Ile Gly Phe Arg Gln Trp Leu Leu Asp Asn 130 135 140 Gly Tyr Thr Ser Ala Ala Thr Glu Ile Val Trp Pro Leu Val Arg Asn 145 150 155 160 Asp Leu Ser Tyr Val Ala Gln Tyr Trp Asn Gln Thr Gly Tyr Asp Leu 165 170 175 Trp Glu Glu Val Asn Gly Ser Ser Phe Phe Thr Ile Ala Val Gln His 180 185 190 Arg Ala Leu Val Glu Gly Ser Ala Phe Ala Thr Ala Val Gly Ser Ser 195 200 205 Cys Ser Trp Cys Asp Ser Gln Ala Pro Gln Ile Leu Cys Tyr Leu Gln 210 215 220 Ser Phe Trp Thr Gly Glu Tyr Ile Leu Ala Asn Phe Asp Ser Ser Arg 225 230 235 240 Ser Gly Lys Asp Thr Asn Thr Leu Leu Gly Ser Ile His Thr Phe Asp 245 250 255 Pro Glu Ala Gly Cys Asp Asp Ser Thr Phe Gln Pro Cys Ser Pro Arg 260 265 270 Ala Leu Ala Asn His Lys Glu Val Val Asp Ser Phe Arg Ser Ile Tyr 275 280 285 Thr Leu Asn Asp Gly Leu Ser Asp Ser Glu Ala Val Ala Val Gly Arg 290 295 300 Tyr Pro Lys Asp Ser Tyr Tyr Asn Gly Asn Pro Trp Phe Leu Cys Thr 305 310 315 320 Leu Ala Ala Ala Glu Gln Leu Tyr Asp Ala Leu Tyr Gln Trp Asp Lys 325 330 335 Gln Gly Ser Leu Glu Ile Thr Asp Val Ser Leu Asp Phe Phe Gln Ala 340 345 350 Leu Tyr Ser Asp Ala Ala Thr Gly Thr Tyr Ser Ser Ser Ser Ser Thr 355 360 365 Tyr Ser Ser Ile Val Asp Ala Val Lys Thr Phe Ala Asp Gly Phe Val 370 375 380 Ser Ile Val Glu Thr His Ala Ala Ser Asn Gly Ser Leu Ser Glu Gln 385 390 395 400 Tyr Asp Lys Ser Asp Gly Asp Glu Leu Ser Ala Arg Asp Leu Thr Trp 405 410 415 Ser Tyr Ala Ala Leu Leu Thr Ala Asn Asn Arg Arg Asn Ser Val Met 420 425 430 Pro Pro Ser Trp Gly Glu Thr Ser Ala Ser Ser Val Pro Gly Thr Cys 435 440 445 SEQ ID NO: 6: <210> 6 <211> 449 <212> PRT <213> <400> 6 Ala Thr Leu Asp Ser Trp Leu Ser Asn Glu Ala Thr Val Ala Arg Thr 1 5 10 15 Ala Ile Leu Asn Asn Ile Gly Ala Asp Gly Ala Trp Val Ser Gly Ala 20 25 30 Asp Ser Gly Ile Val Val Ala Ser Pro Ser Thr Asp Asn Pro Asp Tyr 35 40 45 Phe Tyr Thr Trp Thr Arg Asp Ser Gly Leu Val Leu Lys Thr Leu Val 50 55 60 Asp Leu Phe Arg Asn Gly Asp Thr Ser Leu Leu Ser Thr Ile Glu Asn 65 70 75 80 Tyr Ile Ser Ala Gln Ala Ile Val Gln Gly Ile Ser Asn Pro Ser Gly 85 90 95 Asp Leu Ser Ser Gly Ala Gly Leu Gly Glu Pro Lys Phe Asn Val Asp 100 105 110 Glu Thr Ala Tyr Thr Gly Ser Trp Gly Arg Pro Gln Arg Asp Gly Pro 115 120 125 Ala Leu Arg Ala Thr Ala Met Ile Gly Phe Gly Gln Trp Leu Leu Asp 130 135 140 Asn Gly Tyr Thr Ser Thr Ala Thr Asp Ile Val Trp Pro Leu Val Arg 145 150 155 160 Asn Asp Leu Ser Tyr Val Ala Gln Tyr Trp Asn Gln Thr Gly Tyr Asp 165 170 175 Leu Trp Glu Glu Val Asn Gly Ser Ser Phe Phe Thr Ile Ala Val Gln 180 185 190 His Arg Ala Leu Val Glu Gly Ser Ala Phe Ala Thr Ala Val Gly Ser 195 200 205 Ser Cys Ser Trp Cys Asp Ser Gln Ala Pro Glu Ile Leu Cys Tyr Leu 210 215 220 Gln Ser Phe Trp Thr Gly Ser Phe Ile Leu Ala Asn Phe Asp Ser Ser 225 230 235 240 Arg Ser Gly Lys Asp Ala Asn Thr Leu Leu Gly Ser Ile His Thr Phe 245 250 255 Asp Pro Glu Ala Ala Cys Asp Asp Ser Thr Phe Gln Pro Cys Ser Pro 260 265 270 Arg Ala Leu Ala Asn His Lys Glu Val Val Asp Ser Phe Arg Ser Ile 275 280 285 Tyr Thr Leu Asn Asp Gly Leu Ser Asp Ser Glu Ala Val Ala Val Gly 290 295 300 Arg Tyr Pro Glu Asp Thr Tyr Tyr Asn Gly Asn Pro Trp Phe Leu Cys 305 310 315 320 Thr Leu Ala Ala Ala Glu Gln Leu Tyr Asp Ala Leu Tyr Gln Trp Asp 325 330 335 Lys Gln Gly Ser Leu Glu Val Thr Asp Val Ser Leu Asp Phe Phe Lys 340 345 350 Ala Leu Tyr Ser Asp Ala Ala Thr Gly Thr Tyr Ser Ser Ser Ser Ser 355 360 365 Thr Tyr Ser Ser Ile Val Asp Ala Val Lys Thr Phe Ala Asp Gly Phe 370 375 380 Val Ser Ile Val Glu Thr His Ala Ala Ser Asn Gly Ser Met Ser Glu 385 390 395 400 Gln Tyr Asp Lys Ser Asp Gly Glu Gln Leu Ser Ala Arg Asp Leu Thr 405 410 415 Trp Ser Tyr Ala Ala Leu Leu Thr Ala Asn Asn Arg Arg Asn Ser Val 420 425 430 Val Pro Ala Ser Trp Gly Glu Thr Ser Ala Ser Ser Val Pro Gly Thr 435 440 445 Cys SEQ ID NO: 7: <210> 7 <211> 450 <212> PRT <213> <400> 7 Gln Ser Asp Leu Asn Ala Phe Ile Glu Ala Gln Thr Pro Ile Ala Lys 1 5 10 15 Gln Gly Tyr Leu Asn Asn Ile Gly Ala Asp Gly Lys Leu Val Glu Gly 20 25 30 Ala Ala Ala Gly Ile Val Tyr Ala Ser Pro Ser Lys Ser Asn Pro Asp 35 40 45 Tyr Phe Tyr Thr Trp Thr Arg Asp Ala Gly Leu Thr Met Glu Glu Tyr 50 55 60 Ile Glu Gln Phe Ile Gly Gly Asp Ala Thr Leu Glu Ser Thr Ile Gln 65 70 75 80 Asn Tyr Val Asp Ser Gln Ala Asn Glu Gln Ala Val Ser Asn Pro Ser 85 90 95 Gly Gly Leu Ser Asp Gly Ser Gly Leu Ala Glu Pro Lys Phe Tyr Tyr 100 105 110 Asn Ile Ser Gln Phe Thr Asp Ser Trp Gly Arg Pro Gln Arg Asp Gly 115 120 125 Pro Ala Leu Arg Ala Ser Ala Leu Ile Ala Tyr Gly Asn Ser Leu Ile 130 135 140 Ser Ser Asp Lys Gln Ser Val Val Lys Ala Asn Ile Trp Pro Ile Tyr 145 150 155 160 Gln Asn Asp Leu Ser Tyr Val Gly Gln Tyr Trp Asn Gln Thr Gly Phe 165 170 175 Asp Leu Trp Glu Glu Val Gln Gly Ser Ser Phe Phe Thr Val Ala Val 180 185 190 Gln His Lys Ala Leu Val Glu Gly Asp Ala Phe Ala Lys Ala Leu Gly 195 200 205 Glu Glu Cys Gln Ala Cys Ser Val Ala Pro Gln Ile Leu Cys His Leu 210 215 220 Gln Asp Phe Trp Asn Gly Ser Ala Val Leu Ser Asn Leu Pro Thr Asn 225 230 235 240 Gly Arg Ser Gly Leu Asp Thr Asn Ser Leu Leu Gly Ser Ile His Thr 245 250 255 Phe Asp Pro Ala Ala Ala Cys Asp Asp Thr Thr Phe Gln Pro Cys Ser 260 265 270 Ser Arg Ala Leu Ser Asn His Lys Leu Val Val Asp Ser Phe Arg Ser 275 280 285 Val Tyr Gly Ile Asn Asn Gly Arg Gly Ala Gly Lys Ala Ala Ala Val 290 295 300 Gly Pro Tyr Ala Glu Asp Thr Tyr Gln Gly Gly Asn Pro Trp Tyr Leu 305 310 315 320 Thr Thr Leu Val Ala Ala Glu Leu Leu Tyr Asp Ala Leu Tyr Gln Trp 325 330 335 Asp Lys Gln Gly Gln Val Asn Val Thr Glu Thr Ser Leu Pro Phe Phe 340 345 350 Lys Asp Leu Ser Ser Asn Val Thr Thr Gly Ser Tyr Ala Lys Ser Ser 355 360 365 Ser Ala Tyr Glu Ser Leu Thr Ser Ala Val Lys Thr Tyr Ala Asp Gly 370 375 380 Phe Ile Ser Val Val Gln Glu Tyr Thr Pro Asp Gly Gly Ala Leu Ala 385 390 395 400 Glu Gln Tyr Ser Arg Asp Gln Gly Thr Pro Val Ser Ala Ser Asp Leu 405 410 415 Thr Trp Ser Tyr Ala Ala Phe Leu Ser Ala Val Gly Arg Arg Asn Gly 420 425 430 Thr Val Pro Ala Ser Trp Gly Ser Ser Thr Ala Asn Ala Val Pro Ser 435 440 445 Gln Cys 450 SEQ ID NO: 8: <210> 8 <211> 441 <212> PRT <213> <400> 8 Ala Ala Val Asp Thr Phe Ile Asn Thr Glu Lys Pro Ile Ala Trp Asn 1 5 10 15 Lys Leu Leu Ala Asn Ile Gly Pro Asn Gly Lys Ala Ala Pro Gly Ala 20 25 30 Ala Ala Gly Val Val Ile Ala Ser Pro Ser Arg Thr Asp Pro Pro Tyr 35 40 45 Phe Phe Thr Trp Thr Pro Asp Ala Ala Leu Val Leu Thr Gly Ile Ile 50 55 60 Glu Ser Leu Gly His Asn Tyr Asn Thr Thr Leu Gln Gln Val Ser Asn 65 70 75 80 Pro Ser Gly Thr Phe Ala Asp Gly Ser Gly Leu Gly Glu Ala Lys Phe 85 90 95 Asn Val Asp Leu Thr Ala Phe Thr Gly Glu Trp Gly Arg Pro Gln Arg 100 105 110 Asp Gly Pro Pro Leu Arg Ala Ile Ala Leu Ile Gln Tyr Ala Lys Trp 115 120 125 Leu Ile Ala Asn Gly Tyr Lys Ser Thr Ala Lys Ser Val Val Trp Pro 130 135 140 Val Val Lys Asn Asp Leu Ala Tyr Thr Ala Gln Tyr Trp Asn Glu Thr 145 150 155 160 Gly Phe Asp Leu Trp Glu Glu Val Pro Gly Ser Ser Phe Phe Thr Ile 165 170 175 Ala Ser Ser His Arg Ala Leu Thr Glu Gly Ala Tyr Leu Ala Ala Gln 180 185 190 Leu Asp Thr Glu Cys Pro Pro Cys Thr Thr Val Ala Pro Gln Val Leu 195 200 205 Cys Phe Gln Gln Ala Phe Trp Asn Ser Lys Gly Asn Tyr Val Val Ser 210 215 220 Thr Ser Thr Ala Gly Glu Tyr Arg Ser Gly Lys Asp Ala Asn Ser Ile 225 230 235 240 Leu Ala Ser Ile His Asn Phe Asp Pro Glu Ala Gly Cys Asp Asn Leu 245 250 255 Thr Phe Gln Pro Cys Ser Glu Arg Ala Leu Ala Asn His Lys Ala Tyr 260 265 270 Val Asp Ser Phe Arg Asn Leu Tyr Ala Ile Asn Lys Gly Ile Ala Gln 275 280 285 Gly Lys Ala Val Ala Val Gly Arg Tyr Ser Glu Asp Val Tyr Tyr Asn 290 295 300 Gly Asn Pro Trp Tyr Leu Ala Asn Phe Ala Ala Ala Glu Gln Leu Tyr 305 310 315 320 Asp Ala Ile Tyr Val Trp Asn Lys Gln Gly Ser Ile Thr Val Thr Ser 325 330 335 Val Ser Leu Pro Phe Phe Arg Asp Leu Val Ser Ser Val Ser Thr Gly 340 345 350 Thr Tyr Ser Lys Ser Ser Ser Thr Phe Thr Asn Ile Val Asn Ala Val 355 360 365 Lys Ala Tyr Ala Asp Gly Phe Ile Glu Val Ala Ala Lys Tyr Thr Pro 370 375 380 Ser Asn Gly Ala Leu Ala Glu Gln Tyr Asp Arg Asn Thr Gly Lys Pro 385 390 395 400 Asp Ser Ala Ala Asp Leu Thr Trp Ser Tyr Ser Ala Phe Leu Ser Ala 405 410 415 Ile Asp Arg Arg Ala Gly Leu Val Pro Pro Ser Trp Arg Ala Ser Val 420 425 430 Ala Lys Ser Gln Leu Pro Ser Thr Cys 435 440 SEQ ID NO: 9: <210> 9 <211> 452 <212> PRT <213> <400> 9 Ser Val Asp Asp Phe Ile Asn Thr Gln Thr Pro Ile Ala Leu Asn Asn 1 5 10 15 Leu Leu Cys Asn Val Gly Pro Asp Gly Cys Arg Ala Phe Gly Thr Ser 20 25 30 Ala Gly Ala Val Ile Ala Ser Pro Ser Thr Thr Asp Pro Asp Tyr Tyr 35 40 45 Tyr Met Trp Thr Arg Asp Ser Ala Leu Val Phe Lys Asn Ile Val Asp 50 55 60 Arg Phe Thr Gln Gln Tyr Asp Ala Gly Leu Gln Arg Arg Ile Glu Gln 65 70 75 80 Tyr Ile Ser Ala Gln Val Thr Leu Gln Gly Ile Ser Asn Pro Ser Gly 85 90 95 Ser Leu Ser Asp Gly Ser Gly Leu Gly Glu Pro Lys Phe Glu Leu Thr 100 105 110 Leu Ser Gln Phe Thr Gly Asn Trp Gly Arg Pro Gln Arg Asp Gly Pro 115 120 125 Ala Leu Arg Ala Ile Ala Leu Ile Gly Tyr Ser Lys Trp Leu Ile Asn 130 135 140 Asn Asn Tyr Gln Ser Thr Val Ser Asn Ile Ile Trp Pro Ile Val Arg 145 150 155 160 Asn Asp Leu Asn Tyr Val Ala Gln Tyr Trp Asn Gln Thr Gly Phe Asp 165 170 175 Leu Trp Glu Glu Val Asn Gly Ser Ser Phe Phe Thr Val Ala Asn Gln 180 185 190 His Arg Ala Leu Val Glu Gly Ala Thr Leu Ala Ala Thr Leu Gly Gln 195 200 205 Ser Gly Ser Thr Tyr Ser Ser Val Ala Pro Gln Ile Leu Cys Phe Leu 210 215 220 Gln Arg Phe Trp Val Ser Gly Gly Tyr Ile Asp Ser Asn Ile Asn Thr 225 230 235 240 Asn Glu Gly Arg Thr Gly Lys Asp Ala Asn Ser Leu Leu Ala Ser Ile 245 250 255 His Thr Phe Asp Pro Ser Leu Gly Cys Asp Ala Ser Thr Phe Gln Pro 260 265 270 Cys Ser Asp Lys Ala Leu Ser Asn Leu Lys Val Val Val Asp Her Phe 275 280 285 Arg Ser Ile Tyr Gly Val Asn Lys Gly Ile Pro Ala Gly Ser Ala Val 290 295 300 Ala Ile Gly Arg Tyr Pro Glu Asp Val Tyr Phe Asn Gly Asn Pro Trp 305 310 315 320 Tyr Leu Ala Thr Phe Ala Ala Ala Glu Gln Leu Tyr Asp Ser Val Tyr 325 330 335 Val Trp Lys Lys Thr Gly Ser Ile Thr Val Thr Ser Thr Ser Ser Ala 340 345 350 Phe Phe Gln Glu Leu Val Pro Gly Val Ala Ala Gly Thr Tyr Ser Ser 355 360 365 Ser Gln Ser Thr Phe Thr Ser Ile Ile Asn Ala Ile Ser Thr Tyr Ala 370 375 380 Asp Gly Phe Leu Ser Glu Ala Ala Lys Tyr Val Pro Ala Asp Gly Ser 385 390 395 400 Leu Ala Glu Gln Phe Asp Arg Asn Thr Gly Thr Pro Leu Ser Ala Val 405 410 415 His Leu Thr Trp Ser Tyr Ala Ser Phe Leu Thr Ala Ala Ala Arg Arg 420 425 430 Ala Gly Val Val Pro Pro Ser Trp Ala Ser Ser Gly Ala Asn Thr Val 435 440 445 Pro Ser Ser Cys 450 SEQ ID NO: 10: TrGA, linker region <210> 10 <211> 37 <212> PRT <213> <400> 10 Ser Gly Ala Ser Val Val Gly Ser Tyr Ser Arg Pro Thr Ala Thr Ser 1 5 10 15 Phe Pro Pro Ser Gln Thr Pro Lys Pro Gly Val Pro Ser Gly Thr Pro 20 25 30 Tyr Thr Pro Leu Pro 35 SEQ ID NO: 11: TrGA, SBD <210> 11 <211> 109 <212> PRT <213> <400> 11 Cys Ala Thr Pro Thr Ser Val Ala Val Thr Phe His Glu Leu Val Ser 1 5 10 15 Thr Gln Phe Gly Gln Thr Val Lys Val Ala Gly Asn Ala Ala Ala Leu 20 25 30 Gly Asn Trp Ser Thr Ser Ala Ala Val Ala Leu Asp Ala Val Asn Tyr 35 40 45 Ala Asp Asn His Pro Leu Trp Ile Gly Thr Val Asn Leu Glu Ala Gly 50 55 60 Asp Val Val Glu Tyr Lys Tyr Ile Asn Val Gly Gln Asp Gly Ser Val 65 70 75 80 Thr Trp Glu Ser Asp Pro Asn His Thr Tyr Thr Val Pro Ala Val Ala 85 90 95 Cys Val Thr Gln Val Val Lys Glu Asp Thr Trp Gln Ser 100 105 SEQ ID NO: 12 SVDDFI: start of the TrGA mature protein <210> 12 <211> 6 <212> PRT <213> <400> 12 Ser Val Asp Asp Phe Ile 1 5 SEQ ID NO: 384 <210> 384 <211> 588 <212> PRT <213> <400> 384 Gly Ser Leu Asp Ser Phe Leu Ala Thr Glu Thr Pro Ile Ala Leu Gln 1 5 10 15 Gly Val Leu Asn Asn Ile Gly Pro Asn Gly Ala Asp Val Ala Gly Ala 20 25 30 Ser Ala Gly Ile Val Val Ala Ser Pro Ser Arg Ser Asp Pro Asp Tyr 35 40 45 Phe Tyr Ser Trp Thr Arg Asp Ala Ala Leu Thr Ala Lys Tyr Leu Val 50 55 60 Asp Ala Phe Ile Ala Gly Asn Lys Asp Leu Glu Gln Thr Ile Gln Glu 65 70 75 80 Tyr Ile Ser Ala Gln Ala Gln Val Gln Thr Ile Ser Asn Pro Ser Gly 85 90 95 Asp Leu Ser Thr Gly Gly Leu Gly Glu Pro Lys Phe Asn Val Asn Glu 100 105 110 Thr Ala Phe Thr Gly Pro Trp Gly Arg Pro Gln Arg Asp Gly Pro Ala 115 120 125 Leu Arg Ala Thr Ala Leu Ile Ala Tyr Ala Asn Tyr Leu Ile Asp Asn 130 135 140 Gly Gln Ala Ser Thr Ala Asp Glu Ile Ile Trp Pro Ile Val Gln Asn 145 150 155 160 Asp Leu Ser Tyr Val Thr Gln Tyr Trp Asn Ser Ser Thr Phe Asp Leu 165 170 175 Trp Glu Glu Val Glu Gly Ser Ser Phe Phe Thr Thr Ala Val Gln His 180 185 190 Arg Ala Leu Val Glu Gly Asn Ala Leu Ala Thr Arg Leu Asn His Thr 195 200 205 Cys Pro Asn Cys Val Ser Gln Ala Pro Gln Val Leu Cys Phe Leu Gln 210 215 220 Ser Tyr Trp Thr Gly Ser Tyr Val Leu Ala Asn Phe Gly Gly Ser Gly 225 230 235 240 Arg Ser Gly Lys Asp Val Asn Ser Ile Leu Gly Ser Ile His Thr Phe 245 250 255 Asp Pro Ala Gly Gly Cys Asp Asp Ser Thr Phe Gln Pro Cys Ser Ala 260 265 270 Arg Ala Leu Ala Asn His Lys Val Val Thr Asp Ser Phe Arg Ser Val 275 280 285 Tyr Ala Val Asn Ser Gly Ile Ala Glu Gly Ser Ala Val Ala Val Gly 290 295 300 Arg Tyr Pro Glu Asp Val Tyr Gln Gly Gly Asn Pro Trp Tyr Leu Ala 305 310 315 320 Thr Ala Ala Ala Ala Glu Gln Leu Tyr Asp Ala Ile Tyr Gln Trp Asn 325 330 335 Lys Ile Gly Ser Ile Ser Ile Thr Asp Val Ser Leu Ala Phe Phe Gln 340 345 350 Asp Ile Tyr Pro Ser Ala Ala Val Gly Thr Tyr Asn Ser Gly Ser Ser 355 360 365 Thr Phe Asn Asp Ile Ile Ser Ala Val Gln Thr Tyr Ala Asp Gly Tyr 370 375 380 Leu Ser Ile Ile Glu Lys Tyr Thr Pro Ser Asp Gly Ser Leu Thr Glu 385 390 395 400 Gln Phe Ser Arg Ser Asp Gly Thr Pro Leu Ser Ala Ser Gly Leu Thr 405 410 415 Trp Ser Tyr Ala Ser Leu Leu Thr Ala Ala Ala Arg Arg Gln Ser Ile 420 425 430 Val Pro Ala Ser Trp Gly Glu Ser Ser Ala Ser Ser Val Pro Ala Val 435 440 445 Cys Ser Ala Thr Ser Ala Thr Gly Pro Tyr Ser Thr Ala Thr Asn Thr 450 455 460 Ala Trp Pro Ser Ser Gly Ser Gly Pro Ser Thr Thr Thr Ser Val Pro 465 470 475 480 Cys Thr Thr Pro Thr Ser Val Ala Val Thr Phe Asp Glu Ile Val Ser 485 490 495 Thr Thr Tyr Gly Glu Thr Ile Tyr Leu Ala Gly Ser Ile Pro Glu Leu 500 505 510 Gly Asn Trp Ser Pro Ser Ser Ala Ile Pro Leu Arg Ala Asp Ala Tyr 515 520 525 Thr Ser Ser Asn Pro Leu Trp Tyr Val Thr Leu Asn Leu Pro Ala Gly 530 535 540 Thr Ser Phe Glu Tyr Lys Phe Phe Lys Lys Glu Thr Asp Gly Thr Ile 545 550 555 560 Val Trp Glu Asp Asp Pro Asn Arg Ser Tyr Thr Val Pro Ala Tyr Cys 565 570 575 Gly Gln Thr Thr Ala Ile Leu Asp Asp Ser Trp Gln 580 585 SEQ ID NO: 385 <210> 385 <211> 112 <212> PRT <213> <400> 385 Cys Ala Asp Ala Ser Glu Val Tyr Val Thr Phe Asn Glu Arg Val Ser 1 5 10 15 Thr Ala Trp Gly Glu Thr Ile Lys Val Val Gly Asn Val Pro Ala Leu 20 25 30 Gly Asn Trp Asp Thr Ser Lys Ala Val Thr Leu Ser Ala Ser Gly Tyr 35 40 45 Lys Ser Asn Asp Pro Leu Trp Ser Ile Thr Val Pro Ile Lys Ala Thr 50 55 60 Gly Ser Ala Val Gln Tyr Lys Tyr Ile Lys Val Gly Thr Asn Gly Lys 65 70 75 80 Ile Thr Trp Glu Ser Asp Pro Asn Arg Ser Ile Thr Leu Gln Thr Ala 85 90 95 Ser Ser Ala Gly Lys Cys Ala Ala Gln Thr Val Asn Asp Ser Trp Arg 100 105 110 SEQ ID NO: 386 <210> 386 <211> 109 <212> PRT <213> <400> 386 Cys Thr Pro Pro Ser Glu Val Thr Leu Thr Phe Asn Ala Leu Val Asp 1 5 10 15 Thr Ala Phe Gly Gln Asn Ile Tyr Leu Val Gly Ser Ile Pro Glu Leu 20 25 30 Gly Ser Trp Asp Pro Ala Asn Ala Leu Leu Met Ser Ala Lys Ser Trp 35 40 45 Thr Ser Gly Asn Pro Val Trp Thr Leu Ser Ile Ser Leu Pro Ala Gly 50 55 60 Thr Ser Phe Glu Tyr Lys Phe Ile Arg Lys Asp Asp Gly Ser Ser Asp 65 70 75 80 Val Val Trp Glu Ser Asp Pro Asn Arg Ser Tyr Asn Val Pro Lys Asp 85 90 95 Cys Gly Ala Asn Thr Ala Thr Val Asn Ser Trp Trp Arg 100 105 SEQ ID NO: 387 <210> 387 <211> 108 <212> PRT <213> <400> 387 Cys Thr Thr Pro Thr Ser Val Ala Val Thr Phe Asp Glu Ile Val Ser 1 5 10 15 Thr Ser Tyr Gly Glu Thr Ile Tyr Leu Ala Gly Ser Ile Pro Glu Leu 20 25 30 Gly Asn Trp Ser Thr Ala Ser Ala Ile Pro Leu Arg Ala Asp Ala Tyr 35 40 45 Thr Asn Ser Asn Pro Leu Trp Tyr Val Thr Val Asn Leu Pro Pro Gly 50 55 60 Thr Ser Phe Glu Tyr Lys Phe Phe Lys Asn Gln Thr Asp Gly Thr Ile 65 70 75 80 Val Trp Glu Asp Asp Pro Asn Arg Ser Tyr Thr Val Pro Ala Tyr Cys 85 90 95 Gly Gln Thr Thr Ala Ile Leu Asp Asp Ser Trp Gln 100 105 SEQ ID NO: 388 <210> 388 <211> 108 <212> PRT <213> <400> 388 Cys Thr Thr Pro Thr Ala Val Ala Val Thr Phe Asp Leu Thr Ala Thr 1 5 10 15 Thr Thr Tyr Gly Glu Asn Ile Tyr Leu Val Gly Ser Ile Ser Gln Leu 20 25 30 Gly Asp Trp Glu Thr Ser Asp Gly Ile Ala Leu Ser Ala Asp Lys Tyr 35 40 45 Thr Ser Ser Asp Pro Leu Trp Tyr Val Thr Val Thr Leu Pro Ala Gly 50 55 60 Glu Ser Phe Glu Tyr Lys Phe Ile Arg Ile Glu Ser Asp Asp Ser Val 65 70 75 80 Glu Trp Glu Ser Asp Pro Asn Arg Glu Tyr Thr Val Pro Gln Ala Cys 85 90 95 Gly Thr Ser Thr Ala Thr Val Thr Asp Thr Trp Arg 100 105 SEQ ID NO: 389 <210> 389 <211> 108 <212> PRT <213> <400> 389 Cys Thr Thr Pro Thr Ala Val Ala Val Thr Phe Asp Leu Thr Ala Thr 1 5 10 15 Thr Thr Tyr Gly Glu Asn Ile Tyr Leu Val Gly Ser Ile Ser Gln Leu 20 25 30 Gly Asp Trp Asp Thr Ser Asp Gly Ile Ala Leu Ser Ala Asp Lys Tyr 35 40 45 Thr Ser Ser Asn Pro Leu Trp Tyr Val Thr Val Thr Leu Pro Ala Gly 50 55 60 Glu Ser Phe Glu Tyr Lys Phe Ile Arg Ile Glu Ser Asp Asp Ser Val 65 70 75 80 Glu Trp Glu Ser Asp Pro Asn Arg Glu Tyr Thr Val Pro Gln Ala Cys 85 90 95 Gly Glu Ser Thr Ala Thr Val Thr Asp Thr Trp Arg 100 105 SEQ ID NO: 390 <210> 390 <211> 108 <212> PRT <213> <400> 390 Cys Ser Thr Pro Thr Ala Val Ala Val Thr Phe Asn Glu Arg Val Thr 1 5 10 15 Thr Gln Trp Gly Gln Thr Ile Lys Val Val Gly Asp Ala Ala Ala Leu 20 25 30 Gly Gly Trp Asp Thr Ser Lys Ala Val Pro Leu Ser Ala Ala Gly Tyr 35 40 45 Thr Ala Ser Asp Pro Leu Trp Ser Gly Thr Val Asp Leu Pro Ala Gly 50 55 60 Leu Ala Val Gln Tyr Lys Tyr Ile Asn Val Ala Ala Asp Gly Gly Val 65 70 75 80 Thr Trp Glu Ala Asp Pro Asn His Ser Phe Thr Val Pro Ala Ala Cys 85 90 95 Gly Thr Thr Ala Val Thr Arg Asp Asp Thr Trp Gln 100 105 SEQ ID NO: 1098 SVDDFISTETPIALNNLLCNVGPDGCRAFGTSAGAVIASPSTIRPDYYYMWTRDSALVFKNLIDRFTETYDAGLQRRIE QYITAQVTLQGLSNPSGSLADGSGLGEPKFELTLKPFTGNWGRPQRDGPALRAIALIGYSKWLINNNYQSTVSNVIWPI VRNDLNYVAQYWNQTGFDLWEEVNGSSFFTVANQHRALVEGATLAATLGQSGSAYSSVAPQVLCFLQRFWVSSGGYVDS NINTNEGRTGKDVNSVLTSIHTFDPNLGCDAGTFQPCSDKALSNLKVVVDSFRSIYGVNKGIPAGAAVAIGRYAEDVYY NGNPWYLATFAAAEQLYDAIYVWKKTGSITVTATSLAFFQELVPGVTAGTYSSSSSTFTNIINAVSTYADGFLSEAAKY VPADGSLAEQFDRNSGTPLSALHLTWSYASFLTATARRAGIVPPSWANSSASTIPSTCSGASVVGSYSRPTATSFPPSQ TPKPGVPSGTPYTPLPCATPTSVAVTFHELVSTQFGQTVKVAGNAAALGNWSTSAAVALDAVNYRDNHPLWIGTVNLEA GDVVEYKYINVGQDGSVTWESDPNHTYTVPAVACVTQVVKEDTWQS SEQ ID NO: 1099 SVDDFISTETPIALNNLLCNVGPDGCRAFGTSAGAVIASPSTIRPDYYYMWTRDSALVFKILIDRFTETYDAGLQRRIE QYITAQVTLQGLSNPSGSLADGSGLGEPKFELTLKPFTGNWGRPQRDGPALRAIALIGYSKWLINNNYQSTVSNVIWPI VRNDLNYVAQYWNQTGFDLWEEVNGSSFFTVANQHRALVEGATLAATLGQSGSAYSSVAPQVLCFLQRFWVSSGGYVDS NINTNEGRTGKDVNSVLTSIHTFDPNLGCDAGTFQPCSDKALSNLKVVVDSFRSIYGVNKGIPAGAAVAIGRYAEDVYY NGNPWYLATFAAAEQLYDAIYVWKKTGSITVTATSLAFFQELVPGVTAGTYSSSSSTFTNIINAVSTYADGFLSEAAKY VPADGSLAEQFDRNSGTPLSALHLTWSYASFLTATARRAGIVPPSWANSSASTIPSTCSGASVVGSYSRPTATSFPPSQ TPKPGVPSGTPYTPLPCATPTSVAVTFHELVSTQFGQTVKVAGNAAALGNWSTSAAVALDAVNYRDNHPLWIGTVNLEA GDVVEYKYINVGQDGSVTWESDPNHTYTVPAVACVTQVVKEDTWQS