High-Purity Steviol Glycosides

Methods of preparing highly purified steviol glycosides, particularly rebaudiosides A, D and M are described. The methods include utilizing recombinant microorganisms for converting various staring compositions to target steviol glycosides. In addition, novel steviol glycosides reb D2 and reb M2 are disclosed, as are methods of preparing the same. The highly purified rebaudiosides are useful as non-caloric sweetener in edible and chewable compositions such as any beverages, confectioneries, bakery products, cookies, and chewing gums.

Skip to: Description  ·  Claims  · Patent History  ·  Patent History
Description
CROSS REFERENCE TO RELATED APPLICATIONS

This application claims priority to U.S. Provisional Patent Application No. 61/827,922, filed May 28, 2013; U.S. Provisional Patent Application No. 61/843,544, filed Jul. 8, 2013; U.S. Provisional Patent Application No. 61/861,528, filed Aug. 2, 2013; U.S. Provisional Patent Application No. 61/881,166, filed Sep. 23, 2013; U.S. Provisional Patent Application No. 61/885,084, filed Oct. 1, 2013; U.S. Provisional Patent Application No. 61/904,751, filed Nov. 15, 2013; U.S. Provisional Patent Application No. 61/913,482, filed Dec. 9, 2013; U.S. Provisional Patent Application No. 61/921,635, filed Dec. 30, 2013; U.S. Provisional Patent Application No. 61/925,329, filed Jan. 9, 2014 and U.S. Provisional Patent Application No. 61/939,855, filed Feb. 14, 2014. The above-referenced priority documents are incorporated fully herein in their entirety.

TECHNICAL FIELD

The present invention relates to a biocatalytic process for preparing compositions comprising steviol glycosides, including highly purified steviol glycoside compositions. The present invention also relates to novel steviol glycosides, methods for isolation of the same and uses for the novel steviol glycosides.

BACKGROUND OF THE INVENTION

High intensity sweeteners possess a sweetness level that is many times greater than the sweetness level of sucrose. They are essentially non-caloric and are commonly used in diet and reduced-calorie products, including foods and beverages. High intensity sweeteners do not elicit a glycemic response, making them suitable for use in products targeted to diabetics and others interested in controlling for their intake of carbohydrates.

Steviol glycosides are a class of compounds found in the leaves of Stevia rebaudiana Bertoni, a perennial shrub of the Asteraceae (Compositae) family native to certain regions of South America. They are characterized structurally by a single base, steviol, differing by the presence of carbohydrate residues at positions C13 and C19. They accumulate in Stevia leaves, composing approximately 10%-20% of the total dry weight. On a dry weight basis, the four major glycosides found in the leaves of Stevia typically include stevioside (9.1%), rebaudioside A (3.8%), rebaudioside C (0.6-1.0%) and dulcoside A (0.3%). Other known steviol glycosides include rebaudioside B, C, D, E, F and M, steviolbioside and rubusoside.

Although methods are known for preparing steviol glycosides from Stevia rebaudiana, many of these methods are unsuitable for use commercially.

Accordingly, there remains a need for simple, efficient, and economical methods for preparing compositions comprising steviol glycosides, including highly purified steviol glycoside compositions.

Additionally, there remains a need for novel steviol glycosides and methods of preparing and isolating the same.

SUMMARY OF THE INVENTION

The present invention provides a biocatalytic process for preparing a composition comprising a target steviol glycoside comprising contacting a medium containing a starting composition comprising an organic compound comprising at least one carbon atom with a biocatalyst, thereby producing a composition comprising a target steviol glycoside.

In another embodiment, the present invention provides a method for producing a target steviol glycoside comprising contacting an organic compound and at least one enzyme selected from a steviol biosynthesis enzymes and a UDP-glycosyltransferases, thereby producing a composition comprising the target steviol glycoside.

The organic compound comprising at least one carbon atom is the substrate for the biotransformation. In one embodiment, the organic compound is selected from the group consisting of polyols or sugar alcohols, or various carbohydrates. In another embodiment, the organic compound at least one steviol glycoside.

The target steviol glycoside can be any steviol glycoside that is not the same as the substrate steviol glycoside. In one embodiment, the target steviol glycoside is steviolmonoside, steviolbioside, rubusoside, dulcoside B, dulcoside A, rebaudioside B, rebaudioside G, stevioside, rebaudioside C, rebaudioside F, rebaudioside A, rebaudioside I, rebaudioside E, rebaudioside H, rebaudioside L, rebaudioside K, rebaudioside J, rebaudioside M, rebaudioside M2, rebaudioside D, rebaudioside D2, rebaudioside N, rebaudioside O or a synthetic steviol glycoside.

In one embodiment, the target steviol glycoside is stevioside.

In another embodiment, the target steviol glycoside is rebaudioside A.

In still another embodiment, the target steviol glycoside is rebaudioside D.

In yet another embodiment, the target steviol glycoside is rebaudioside M (also known as rebaudioside X).

In a preferred embodiments, the biocatalyst is an enzyme, or a cell comprising one or more enzyme, capable of converting the organic compound to target steviol glycosides. The biocatalyst can be located on the surface and/or inside the cell. The biocatalyst can be provided in the form of a whole cell suspension, a crude lysate or as purified enzyme(s). The biocatalyst can be in free form or immobilized to a solid support made from inorganic or organic materials.

In some embodiments, a microorganism comprises the necessary biocatalyst(s) for converting the organic compound to target steviol glycosides. Accordingly, the present invention also provides a biocatalytic process for preparing a composition comprising a target steviol glycoside by contacting a starting composition comprising an organic compound with a microorganism comprising at least one enzyme capable of converting the organic compound to target steviol glycosides, thereby producing a medium comprising at least one target steviol glycoside.

The enzymes necessary for converting the organic compound to target steviol glycosides include the steviol biosynthesis enzymes, UDP-glycosyltransferases (UGTs) and/or UDP-recycling enzyme.

In one embodiment the steviol biosynthesis enzymes are selected from the group consisting of geranylgeranyl diphosphate synthase, copalyl diphosphate synthase, kaurene synthase, kaurene oxidase, kaurenoic acid 13-hydroxylase (KAH), steviol synthetase, deoxyxylulose 5-phosphate synthase (DXS), D-1-deoxyxylulose 5-phosphate reductoisomerase (DXR), 4-diphosphocytidyl-2-C-methyl-D-erythritol synthase (CMS), 4-diphosphocytidyl-2-C-methyl-D-erythritol kinase (CMK), 4-diphosphocytidyl-2-C-methyl-D-erythritol 2,4-cyclodiphosphate synthase (MCS), 1-hydroxy-2-methyl-2(E)-butenyl 4-diphosphate synthase (HDS), 1-hydroxy-2-methyl-2(E)-butenyl 4-diphosphate reductase (HDR), acetoacetyl-CoA thiolase, truncated HMG-CoA reductase, mevalonate kinase, phosphomevalonate kinase, mevalonate pyrophosphate decarboxylase and cytochrome P450 reductase.

The UDP-glucosyltransferase can be any UDP-glucosyltransferase capable of adding at least one glucose unit to the steviol and or steviol glycoside substrate to provide the target steviol glycoside.

In one embodiment, steviol biosynthesis enzymes and UDP-glucosyltransferases are produced in a microorganism. The microorganism may be, for example, E. coli, Saccharomyces sp., Aspergillus sp., Pichia sp., Bacillus sp., Yarrowia sp. etc. In another embodiment, the UDP-glucosyltransferases are synthesized.

In one embodiment, the UDP-glucosyltransferase is selected from group consisting of UGT74G1, UGT85C2, UGT76G1, UGT91D2, UGTSL, UGTSL_Sc, UGTSL2 (GI No. 460410132 version XP_004250485.1), UGTLB, GI No. 460409128 (UGTSL) version XP_004249992.1, GI No. 115454819 version NP_001051010.1, GI No. 187373030, version ACD03249.1, GI No. 222619587 version EEE55719.1, GI No. 297795735 version XP_002865752.1 or EUGT11 and UGTs having substantial (>85%) identity to these polypeptides as well as isolated nucleic acid molecules that code for these UGTs.

In one embodiment, steviol biosynthesis enzymes, UGTs and UDP-glucose recycling system are present in one microorganism. The microorganism may be for example, E. coli, Saccharomyces sp., Aspergillus sp., Pichia sp., Bacillus sp., Yarrowia sp.

In one embodiment, the UDP-glucosyltransferase is any UDP-glucosyltransferase capable of adding at least one glucose unit to rubusoside to form stevioside. In a particular embodiment, the UDP-glucosyltransferase is UGT91D2.

In one embodiment, the UDP-glucosyltransferase is any UDP-glucosyltransferase capable of adding at least one glucose unit to stevioside to form rebaudioside A. In a particular embodiment, the UDP-glucosyltransferase is UGT76G1.

In another embodiment, the UDP-glucosyltransferase is any UDP-glucosyltransferase capable of adding at least one glucose unit to rebaudioside A to form rebaudioside D. In a particular embodiment, the UDP-glucosyltransferase is UGT91D2. In another embodiment, the UGT is an improved variant of UGT91D2 with higher activity and/or selectivity produced by directed evolution.

In yet another embodiment, the UDP-glucosyltransferase is any UDP-glucosyltransferase capable of adding at least one glucose unit to rebaudioside D to form rebaudioside M. In a particular embodiment, the UDP-glucosyltransferase is UGT76G1. In another embodiment, the UGT is an improved variant of UGT76G1 with higher activity and/or selectivity produced by directed evolution.

Optionally, the method of the present invention further comprises recycling UDP to provide UDP-glucose. In one embodiment, the method comprises recycling UDP by providing a recycling catalyst and a recycling substrate, such that the biotransformation of the steviol glycoside substrate to the target steviol glycoside is carried out using catalytic amounts of UDP-glucosyltransferase and UDP-glucose.

In one embodiment, the recycling catalyst is sucrose synthase.

In one embodiment, the recycling substrate is sucrose.

Optionally, the method of the present invention further comprises separating the target steviol glycoside from the medium to provide a highly purified target steviol glycoside composition. The target steviol glycoside can be separated by at least one suitable method, such as, for example, crystallization, separation by membranes, centrifugation, extraction, chromatographic separation or a combination of such methods.

In one embodiment, the target steviol glycoside can be produced within the microorganism. In another embodiment, the target steviol glycoside can be secreted out in the medium. In one another embodiment, the released steviol glycoside can be continuously removed from the medium. In yet another embodiment, the target steviol glycoside is separated after the completion of the reaction.

In one embodiment, separation produces a composition comprising greater than about 80% by weight of the target steviol glycoside on an anhydrous basis, i.e., a highly purified steviol glycoside composition. In another embodiment, separation produces a composition comprising greater than about 90% by weight of the target steviol glycoside. In particular embodiments, the composition comprises greater than about 95% by weight of the target steviol glycoside. In other embodiments, the composition comprises greater than about 99% by weight of the target steviol glycoside.

The target steviol glycoside can be in any polymorphic or amorphous form, including hydrates, solvates, anhydrous or combinations thereof.

Purified target steviol glycosides can be used in consumable products as a sweetener. Suitable consumer products include, but are not limited to, food, beverages, pharmaceutical compositions, tobacco products, nutraceutical compositions, oral hygiene compositions, and cosmetic compositions.

The present invention also provides steviol glycosides rebaudioside D2 (reb D2, isomer of rebaudioside D) and rebaudioside M2 (reb M2, isomer of rebaudioside M). In one embodiment, isolated and purified reb D2 is provided. In another embodiment, isolated and purified reb M2 is provided. Reb D2 and reb M2 may also be present in any consumable products disclosed herein. In a particular embodiment, beverages comprising reb D2 and/or reb M2 are provided.

Methods of preparing reb D2 and reb M2 are also provided herein. Both are formed during the biotransformation of reb A to reb D. Reb M2 is believed to form from biotransformation of reb D2 in situ.

In one embodiment, the present invention is a method for the preparation of a composition comprising reb D2 comprising: (a) contacting a starting composition comprising reb A with an enzyme capable of transforming reb A to reb D2, UDP-glucose, and optionally UDP-glucose recycling enzymes, to produce a composition comprising reb D2, and (b) isolating the composition comprising reb D2.

In another embodiment, the present invention is a method for the preparation of a composition comprising reb M2 comprising (a) contacting a starting composition comprising reb D2 with an enzyme capable of transforming reb D2 to reb M2, UDP-glucose, and optionally UDP-glucose recycling enzymes, to produce a composition comprising reb M2, and (b) and isolating the composition comprising reb M2.

A further method for the preparation of a composition comprising reb M2 comprises (a) contacting a starting composition comprising reb A with an enzyme capable of transforming reb A to reb D2, UDP-glucose, and optionally UDP-glucose recycling enzymes, to produce a composition comprising reb D2, (b) optionally, isolating the composition comprising reb D2, (c) contacting the composition comprising reb D2 with an enzyme capable of transforming reb D2 to reb M2, UDP-glucose, and optionally UDP-glucose recycling enzymes to produce a composition comprising reb M2, and (d) isolating the composition comprising reb M2.

The composition can be further purified to provide reb D2 or reb M2 with purities greater than about 95% by weight on a dry basis.

BRIEF DESCRIPTION OF THE DRAWINGS

The accompanying drawings are included to provide a further understanding of the invention. The drawings illustrate embodiments of the invention and together with the description serve to explain the principles of the embodiments of the invention.

FIG. 1 shows the biocatalytic production of reb M from stevioside.

FIG. 2 shows the biocatalytic production of reb A from stevioside using the enzyme UGT76G1 and concomitant recycling of UDP to UDP glucose via sucrose synthase.

FIG. 3 shows the HPLC chromatogram of the product of the biocatalytic production of reb M from reb D, as detailed in Example 14. The peak with retention time of 24.165 minutes corresponds to unreacted reb D. The peak with retention time of 31.325 minutes corresponds to reb M.

FIG. 4 shows the UGT76G1 catalyzed transformation of stevioside to reb A.

FIG. 5 shows the UGT76G1 catalyzed transformation of reb D to reb M.

FIG. 6 shows LC-MS analysis of semi-synthetic steviol glycoside mixture, Lot number CB-2977-106, showing TIC (A), MS of peak at 1.8 min (B), MS of reb M2 peak at 4.1 min (C), MS of reb D peak at 6.0 min (D), MS of reb D2 peak at 7.7 min (E), MS of peak at 9.4 min (F), MS of rebaudioside Apeak at 15.2 min (G), MS of peak at 16.5 min (H), and MS of peak at 18.3 min (I).

FIG. 7 shows HPLC analysis of semi-synthetic steviol glycoside mixture, Lot number CB-2977-106 (A), Isolated reb M2 (B), isolated reb D (C) and isolated reb D2 (D).

FIG. 8 shows the 1H NMR spectrum of reb D2 (500 MHz, pyridine-d5).

FIG. 9 shows the 13C NMR spectrum of reb D2 (125 MHz, pyridine-d5).

FIG. 10 shows an expansion of the 13C NMR spectrum of reb D2 (125 MHz, pyridine-d5).

FIG. 11 shows the 1H-1H COSY Spectrum of reb D2 (500 MHz, pyridine-d5).

FIG. 12 shows the HSQC-DEPT spectrum of reb D2 (500 MHz, pyridine-d5).

FIG. 13 shows the HMBC spectrum of reb D2.

FIG. 14 shows an expansion of HMBC spectrum of reb D2 (500 MHz, pyridine-d5).

FIG. 15 shows the NOESY spectrum of reb D2.

FIG. 16 shows 1H NMR spectrum of reb D2 (500 MHz, pyridine-d5) acquired after ˜46 hours.

FIG. 17 shows and expansion of 1H NMR spectrum of reb D2 (500 MHz, pyridine-d5) acquired after ˜46 hours.

FIG. 18 shows the 1H NMR spectrum of reb M2 (500 MHz, D2O).

FIG. 19 shows the 13C NMR spectrum of reb M2 (125 MHz, D2O/TSP).

FIG. 20 shows an expansion of the 13C NMR spectrum of reb M2 (125 MHz, D2O/TSP).

FIG. 21 shows the 1H-1H COSY spectrum of reb M2 (500 MHz, D2O).

FIG. 22 shows the HSQC-DEPT spectrum of reb M2 (500 MHz, D2O).

FIG. 23 shows the HMBC spectrum of reb M2 (500 MHz, D2O).

FIG. 24 shows an expansion of HMBC spectrum of reb M2 (500 MHz, D2O).

 DETAILED DESCRIPTION

The present invention provides a biocatalytic process for preparing a composition comprising a target steviol glycoside by contacting a medium containing a starting composition comprising an organic compound comprising at least one carbon atom with a biocatalyst, thereby producing a medium comprising a target steviol glycoside.

In another embodiment, the present invention provides a method for producing a target steviol glycoside comprising contacting an organic compound and at least one enzyme selected from a steviol biosynthesis enzymes and a UDP-glycosyltransferases, thereby producing a composition comprising the target steviol glycoside.

One object of the invention is to provide an efficient biocatalytic method for preparing steviol glycosides, particularly stevioside, reb E, reb A, reb D, reb D2, reb M, and reb M2 from various organic compounds in starting compositions.

As used herein, “biocatalysis” or “biocatalytic” refers to the use of natural or genetically engineered biocatalysts, such as enzymes, or cells comprising one or more enzyme, capable of single or multiple step chemical transformations on organic compounds. Biocatalysis processes include fermentation, biosynthesis and biotransformation processes. Both isolated enzyme and whole-cell biocatalysis methods are known in the art. Biocatalyst protein enzymes can be naturally occurring or recombinant proteins.

As used herein, the term “steviol glycoside(s)” refers to a glycoside of steviol, including, but not limited to, naturally occurring steviol glycosides, e.g. steviolmonoside, steviolbioside, rubusoside, dulcoside B, dulcoside A, rebaudioside B, rebaudioside G, stevioside, rebaudioside C, rebaudioside F, rebaudioside A, rebaudioside I, rebaudioside E, rebaudioside H, rebaudioside L, rebaudioside K, rebaudioside J, rebaudioside M, rebaudioside M2, rebaudioside D, rebaudioside D2, rebaudioside N, rebaudioside O, synthetic steviol glycosides, e.g. enzymatically glucosylated steviol glycosides and combinations thereof.

Starting Composition

As used herein, “starting composition” refers to any composition (generally an aqueous solution) containing one or more organic compound comprising at least one carbon atom.

In one embodiment, the organic compound is selected from the group consisting of polyols and various carbohydrates. Such organic compounds, and starting compositions comprising the same, are particularly useful when the present method is a fermentation method.

The term “polyol” refers to a molecule that contains more than one hydroxyl group. A polyol may be a diol, triol, or a tetraol which contain 2, 3, and 4 hydroxyl groups, respectively. A polyol also may contain more than four hydroxyl groups, such as a pentaol, hexaol, heptaol, or the like, which contain 5, 6, or 7 hydroxyl groups, respectively. Additionally, a polyol also may be a sugar alcohol, polyhydric alcohol, or polyalcohol which is a reduced form of carbohydrate, wherein the carbonyl group (aldehyde or ketone, reducing sugar) has been reduced to a primary or secondary hydroxyl group. Examples of polyols include, but are not limited to, erythritol, maltitol, mannitol, sorbitol, lactitol, xylitol, inositol, isomalt, propylene glycol, glycerol, threitol, galactitol, hydrogenated isomaltulose, reduced isomalto-oligosaccharides, reduced xylo-oligosaccharides, reduced gentio-oligosaccharides, reduced maltose syrup, reduced glucose syrup, hydrogenated starch hydrolyzates, polyglycitols and sugar alcohols or any other carbohydrates capable of being reduced.

The term “carbohydrate” refers to aldehyde or ketone compounds substituted with multiple hydroxyl groups, of the general formula (CH2O)n, wherein n is 3-30, as well as their oligomers and polymers. The carbohydrates of the present invention can, in addition, be substituted or deoxygenated at one or more positions. Carbohydrates, as used herein, encompass unmodified carbohydrates, carbohydrate derivatives, substituted carbohydrates, and modified carbohydrates. As used herein, the phrases “carbohydrate derivatives”, “substituted carbohydrate”, and “modified carbohydrates” are synonymous. Modified carbohydrate means any carbohydrate wherein at least one atom has been added, removed, or substituted, or combinations thereof. Thus, carbohydrate derivatives or substituted carbohydrates include substituted and unsubstituted monosaccharides, disaccharides, oligosaccharides, and polysaccharides. The carbohydrate derivatives or substituted carbohydrates optionally can be deoxygenated at any corresponding C-position, and/or substituted with one or more moieties such as hydrogen, halogen, haloalkyl, carboxyl, acyl, acyloxy, amino, amido, carboxyl derivatives, alkylamino, dialkylamino, arylamino, alkoxy, aryloxy, nitro, cyano, sulfo, mercapto, imino, sulfonyl, sulfenyl, sulfinyl, sulfamoyl, carboalkoxy, carboxamido, phosphonyl, phosphinyl, phosphoryl, phosphino, thioester, thioether, oximino, hydrazino, carbamyl, phospho, phosphonato, or any other viable functional group provided the carbohydrate derivative or substituted carbohydrate functions to improve the sweet taste of the sweetener composition.

Examples of carbohydrates which may be used in accordance with this invention include, but are not limited to, tagatose, trehalose, galactose, rhamnose, various cyclodextrins, cyclic oligosaccharides, various types of maltodextrins, dextran, sucrose, glucose, ribulose, fructose, threose, arabinose, xylose, lyxose, allose, altrose, mannose, idose, lactose, maltose, invert sugar, isotrehalose, neotrehalose, isomaltulose, erythrose, deoxyribose, gulose, idose, talose, erythrulose, xylulose, psicose, turanose, cellobiose, amylopectin, glucosamine, mannosamine, fucose, glucuronic acid, gluconic acid, glucono-lactone, abequose, galactosamine, beet oligosaccharides, isomalto-oligosaccharides (isomaltose, isomaltotriose, panose and the like), xylo-oligosaccharides (xylotriose, xylobiose and the like), xylo-terminated oligosaccharides, gentio-oligosaccharides (gentiobiose, gentiotriose, gentiotetraose and the like), sorbose, nigero-oligosaccharides, palatinose oligosaccharides, fructooligosaccharides (kestose, nystose and the like), maltotetraol, maltotriol, malto-oligosaccharides (maltotriose, maltotetraose, maltopentaose, maltohexaose, maltoheptaose and the like), starch, inulin, inulo-oligosaccharides, lactulose, melibiose, raffinose, ribose, isomerized liquid sugars such as high fructose corn syrups, coupling sugars, and soybean oligosaccharides. Additionally, the carbohydrates as used herein may be in either the D- or L-configuration.

The starting composition may be synthetic or purified (partially or entirely), commercially available or prepared.

In one embodiment, the organic compound is glycerol. In another embodiment, the starting composition comprises glycerol.

In one embodiment, the organic compound is glucose. In another embodiment, the starting composition comprises glucose.

In one embodiment, the organic compound is sucrose. In another embodiment, the starting composition comprises sucrose.

In one embodiment, the organic compound is starch. In another embodiment, the starting composition comprises starch.

In one embodiment, the organic compound is maltodextrin. In another embodiment, the starting composition comprises maltodextrin.

The organic compound(s) serve as a substrate(s) for the production of the target steviol glycoside(s), as described herein.

The present method also provides methods of biocatalytic conversion one steviol glycoside to another steviol glycoside. Accordingly, in some embodiments, the organic compound is a steviol glycoside including, but not limited to, steviolmonoside, steviolbioside, rubusoside, dulcoside B, dulcoside A, rebaudioside B, rebaudioside G, stevioside, rebaudioside C, rebaudioside F, rebaudioside A, rebaudioside I, rebaudioside E, rebaudioside H, rebaudioside L, rebaudioside K, rebaudioside J, rebaudioside M, rebaudioside M2, rebaudioside D, rebaudioside D2, rebaudioside N or rebaudioside O, or other glycoside of steviol.

Notably, the substrate steviol glycoside for biocatalytic conversion is not the same as the target steviol glycoside, discussed below. However, the starting composition may contain steviol glycosides other than the substrate steviol glycoside and, in some cases, may contain some amount of target steviol glycoside.

Target Steviol Glycoside

The target steviol glycoside of the present method can be any steviol glycoside that can be prepared by the process disclosed herein. In one embodiment, the target steviol glycoside is selected from the group consisting of steviolmonoside, steviolbioside, rubusoside, dulcoside B, dulcoside A, rebaudioside B, rebaudioside G, stevioside, rebaudioside C, rebaudioside F, rebaudioside A, rebaudioside I, rebaudioside E, rebaudioside H, rebaudioside L, rebaudioside K, rebaudioside J, rebaudioside M, rebaudioside M2, rebaudioside D, rebaudioside D2, rebaudioside N or rebaudioside O, or other glycoside of steviol.

In one embodiment, the target steviol glycoside is stevioside. In another embodiment, the target steviol glycoside is reb A. In still another embodiment, the target steviol glycoside is reb E. In yet another embodiment, the target steviol glycoside is reb D. In yet another embodiment, the target steviol glycoside is reb D2. In a further embodiment, the target steviol glycoside is reb M. In a still further another embodiment, the target steviol glycoside is reb M2.

The target steviol glycoside can be in any polymorphic or amorphous form, including hydrates, solvates, anhydrous or combinations thereof.

In one embodiment, the present invention is a biocatalytic process for the production of reb A. In a more particular embodiment, the present invention is a fermentation process for the production of reb A from a starting composition comprising, e.g., glucose.

In another embodiment, the present invention is a biocatalytic process for the production of reb E. In a more particular embodiment, the present invention is a fermentation process for the production of reb E from a starting composition comprising, e.g., glucose.

In still another embodiment, the present invention is a biocatalytic process for the production of reb D. In a more particular embodiment, the present invention is a fermentation process for the production of reb D from a starting composition comprising, e.g., glucose.

In yet another embodiment, the present invention is a biocatalytic process for the production of reb D2. In a more particular embodiment, the present invention is a fermentation process for the production of reb D2 from a starting composition comprising, e.g., glucose.

In a further embodiment, the present invention is a biocatalytic process for the production of reb M. In a more particular embodiment, the present invention is a fermentation process for the production of reb M from a starting composition comprising, e.g., glucose.

In a still further embodiment, the present invention is a biocatalytic process for the production of reb M2. In a more particular embodiment, the present invention is a fermentation process for the production of reb M2 from a starting composition comprising, e.g., glucose.

In another further embodiment, the present invention is a biocatalytic process for the production of stevioside. In a more particular embodiment, the present invention is a fermentation process for the production of stevioside from a starting composition comprising, e.g., glucose.

Optionally, the method of the present invention further comprises separating the target steviol glycoside from the medium to provide a highly purified target steviol glycoside composition. The target steviol glycoside can be separated by any suitable method, such as, for example, crystallization, separation by membranes, centrifugation, extraction, chromatographic separation or a combination of such methods.

In particular embodiments, the process described herein results in a highly purified target steviol glycoside composition. The term “highly purified”, as used herein, refers to a composition having greater than about 80% by weight of the target steviol glycoside on an anhydrous basis. In one embodiment, the highly purified target steviol glycoside composition contains greater than about 90% by weight of the target steviol glycoside on an anhydrous basis, such as, for example, greater than about 91%, greater than about 92%, greater than about 93%, greater than about 94%, greater than about 95%, greater than about 96%, greater than about 97%, greater than about 98% or greater than about 99% target steviol glycoside content on a dry basis.

In one embodiment, when the target steviol glycoside is reb M, the process described herein provides a composition having greater than about 90% reb M content by weight on a dry basis. In another particular embodiment, when the target steviol glycoside is reb M, the process described herein provides a composition comprising greater than about 95% reb M content by weight on a dry basis.

In another embodiment, when the target steviol glycoside is reb M2, the process described herein provides a composition having greater than about 90% reb M2 content by weight on a dry basis. In another particular embodiment, when the target steviol glycoside is reb M2, the process described herein provides a composition comprising greater than about 95% reb M2 content by weight on a dry basis.

In yet another embodiment, when the target steviol glycoside is reb D, the process described herein provides a composition greater than about 90% reb D content by weight on a dry basis. In another particular embodiment, when the target steviol glycoside is reb D, the process described herein provides a composition comprising greater than about 95% reb D content by weight on a dry basis.

In still another embodiment, when the target steviol glycoside is reb D2, the process described herein provides a composition greater than about 90% reb D2 content by weight on a dry basis. In another particular embodiment, when the target steviol glycoside is reb D2, the process described herein provides a composition comprising greater than about 95% reb D2 content by weight on a dry basis.

In a further embodiment, when the target steviol glycoside is reb A, the process described herein provides a composition comprising greater than about 90% reb A content by weight on a dry basis. In another particular embodiment, when the target steviol glycoside is reb A, the process described herein provides a composition comprising greater than about 95% reb A content by weight on a dry basis.

In a still further embodiment, when the target steviol glycoside is reb E, the process described herein provides a composition comprising greater than about 90% reb E content by weight on a dry basis. In another particular embodiment, when the target steviol glycoside is reb E, the process described herein provides a composition comprising greater than about 95% reb E content by weight on a dry basis.

In yet a further embodiment, when the target steviol glycoside is stevioside, the process described herein provides a composition comprising greater than about 90% stevioside content by weight on a dry basis. In another particular embodiment, when the target steviol glycoside is stevioside, the process described herein provides a composition comprising greater than about 95% stevioside content by weight on a dry basis.

Microorganism and Biocatalysts

In one embodiment of present invention, a biocatalyst is contacted with a medium containing the starting composition to produce target steviol glycosides. In certain embodiments, the biocatalyst is an enzyme, or a cell comprising one or more enzyme, capable of converting the organic compound to the target steviol glycoside.

In one embodiment, the biocatalyst is an enzyme capable of converting the organic compound to the target steviol glycoside. The enzyme can be provided in the form of a whole cell suspension, a crude lysate, a purified enzyme or a combination thereof. In one embodiment, the biocatalyst is a purified enzyme capable of converting the organic compound to the target steviol glycoside. In another embodiment, the biocatalyst is a crude lysate comprising at least one enzyme capable of converting the organic compound to the target steviol glycoside. In still another embodiment, the biocatalyst is a whole cell suspension comprising at least one enzyme capable of converting the organic compound to the target steviol glycoside.

In another embodiment, the biocatalyst is one or more cells comprising an enzyme capable of converting the organic compound to the target steviol glycoside. The enzyme can be located on the surface of the cell, inside the cell or located both on the surface of the cell and inside the cell.

In one embodiment, one biocatalyst enzyme is used per conversion of organic compound to target steviol glycoside. In another embodiment, two or more biocatalyst enzymes are used per conversion.

Suitable enzymes for converting the organic compound to target steviol glycosides include, but are not limited to, steviol biosynthesis enzymes and UDP-glycosyltransferases (UGTs).

In one embodiment, the steviol biosynthesis enzymes include mevalonate (MVA) pathway enzymes.

In another embodiment, the steviol biosynthesis enzymes include non-mevalonate 2-C-methyl-D-erythritol-4-phosphate pathway (MEP/DOXP) enzymes.

In one embodiment, the steviol biosynthesis enzymes are selected from the group consisting of geranylgeranyl diphosphate synthase, copalyl diphosphate synthase, kaurene synthase, kaurene oxidase, kaurenoic acid 13-hydroxylase (KAH), steviol synthetase, deoxyxylulose 5-phosphate synthase (DXS), D-1-deoxyxylulose 5-phosphate reductoisomerase (DXR), 4-diphosphocytidyl-2-C-methyl-D-erythritol synthase (CMS), 4-diphosphocytidyl-2-C-methyl-D-erythritol kinase (CMK), 4-diphosphocytidyl-2-C-methyl-D-erythritol 2,4-cyclodiphosphate synthase (MCS), 1-hydroxy-2-methyl-2(E)-butenyl 4-diphosphate synthase (HDS), 1-hydroxy-2-methyl-2(E)-butenyl 4-diphosphate reductase (HDR), acetoacetyl-CoA thiolase, truncated HMG-CoA reductase, mevalonate kinase, phosphomevalonate kinase, mevalonate pyrophosphate decarboxylase and cytochrome P450 reductase.

The UDP-glucosyltransferase can be any UDP-glucosyltransferase capable of adding at least one glucose unit to the steviol and or steviol glycoside substrate to provide the target steviol glycoside.

In one embodiment, the UDP-glucosyltransferase is any UDP-glucosyltransferase capable of adding at least one glucose unit to rubusoside, thereby producing stevioside. The UDP-glucosyltransferase may be, for example, UGT91D2.

In another embodiment, the UDP-glucosyltransferase is any UDP-glucosyltransferase capable of adding at least one glucose unit to rubusoside, thereby producing rebaudioside E. The UDP-glucosyltransferase may be, for example, UGTSL, UGTSL2 or UGTLB.

In still another embodiment, the UDP-glucosyltransferase is any UDP-glucosyltransferase capable of adding at least one glucose unit to rebaudioside E, thereby producing rebaudioside D. The UDP-glucosyltransferase may be, for example, UGT76G1.

In yet embodiment, the UDP-glucosyltransferase is any UDP-glucosyltransferase capable of adding at least one glucose unit to stevioside, thereby producing rebaudioside A. The UDP-glucosyltransferase may be, for example, UGT76G1.

In a further embodiment, the UDP-glucosyltransferase is any UDP-glucosyltransferase capable of adding at least one glucose unit to rebaudioside A, thereby producing rebaudioside D and/or rebaudioside D2 and/or rebaudioside M2. The UDP-glucosyltransferase may be, for example, UGT91D2, UGTSL2, UGTLB or EUGT11.

In another embodiment, the UDP-glucosyltransferase capable of adding at least one glucose unit to rebaudioside A is selected from the following listing of GenInfo identifier numbers, preferably from the group presented in Table 1, and more preferably the group presented in Table 2.

397567 30680413 115480946 147798902 218193594 225443294 454245 32816174 116310259 147811764 218193942 225444853 1359905 32816178 116310985 147827151 219885307 225449296 1685003 34393978 116788066 147836230 222615927 225449700 1685005 37993665 116788606 147839909 222619587 225454338 2191136 37993671 116789315 147846163 222623142 225454340 2501497 37993675 119394507 147855977 222625633 225454342 2911049 39104603 119640480 148905778 222625635 225454473 4218003 41469414 122209731 148905999 222636620 225454475 4314356 41469452 125526997 148906835 222636621 225458362 13492674 42566366 125534279 148907340 222636628 225461551 13492676 42570280 125534461 148908935 222636629 225461556 15217773 42572855 125540090 148909182 224053242 225461558 15217796 44890129 125541516 148909920 224053386 225469538 15223396 46806235 125545408 148910082 224055535 225469540 15223589 50284482 125547340 148910154 224056138 226316457 15227766 51090402 125547520 148910612 224056160 226492603 15230017 51090594 125554547 148910769 224067918 226494221 15231757 52839682 125557592 156138791 224072747 226495389 15234056 56550539 125557593 156138797 224080189 226495945 15234195 62734263 125557608 156138799 224091845 226502400 15234196 62857204 125559566 156138803 224094703 226507980 15238503 62857206 125563266 165972256 224100653 226531147 15239523 62857210 125571055 168016721 224100657 226532094 15239525 62857212 125579728 171674071 224101569 238477377 15239543 75265643 125588307 171906258 224103105 240254512 15239937 75285934 125589492 183013901 224103633 242032615 15240305 75288884 125599469 183013903 224103637 242032621 15240534 77550661 125601477 186478321 224109218 242038423 15982889 77556148 126635837 187373030 224114583 242043290 18086351 82791223 126635845 187373042 224116284 242044836 18418378 83778990 126635847 190692175 224120552 242051252 18418380 89953335 126635863 194701936 224121288 242056217 18418382 110741436 126635867 195620060 224121296 242056219 19743740 110743955 126635883 209954691 224121300 242056663 19911201 115438196 126635887 209954719 224130358 242059339 20149064 115438785 133874210 209954725 224140703 242059341 20260654 115441237 133874212 209954733 224143404 242060922 21435782 115454819 145358033 210063105 224143406 242067411 21553613 115456047 147772508 210063107 224144306 242067413 21593514 115457492 147776893 212275846 224285244 242076258 22759895 115459312 147776894 216296854 225431707 242076396 23955910 115464719 147776895 217074506 225435532 242084750 26452040 115471069 147786916 218185693 225436321 242091005 28393204 115471071 147798900 218187075 225440041 242095206 30679796 115474009 147798901 218189427 225441116 242345159 242345161 297724601 326492035 356523945 357140904 359486938 255536859 297725463 326493430 356523957 357165849 359487055 255538228 297728331 326500410 356523959 357165852 359488135 255541676 297738632 326506816 356523961 357168415 359488708 255547075 297745347 326507826 356523963 357437837 359493630 255552620 297745348 326508394 356524387 357442755 359493632 255552622 297795735 326509445 356524403 357442757 359493634 255555343 297796253 326511261 356527181 357445729 359493636 255555361 297796257 326511866 356533209 357445731 359493815 255555363 297796261 326512412 356533852 357445733 359495856 255555365 297797587 326517673 356534718 357446799 359495858 255555369 297798502 326518800 356535480 357446805 359495869 255555373 297799226 326521124 356542996 357452779 359495871 255555377 297805988 326525567 356543136 357452781 359497638 255556812 297807499 326525957 356543932 357452783 359807261 255556818 297809125 326526607 356549841 357452787 374256637 255563008 297809127 326527141 356549843 357452789 377655465 255564074 297811403 326530093 356554358 357452791 378405177 255564531 297820040 326534036 356554360 357452797 378829085 255572878 297821483 326534312 356558606 357452799 387135070 255577901 297825217 332071132 356560333 357470367 387135072 255583249 297832276 339715876 356560599 357472193 387135078 255583253 297832280 342306012 356560749 357472195 387135092 255583255 297832518 342306016 356566018 357474295 387135094 255585664 297832520 343457675 356566169 357474493 387135098 255585666 297840825 343457677 356566173 357474497 387135100 255634688 297840827 350534960 356567761 357474499 387135134 255644801 297847402 356498085 356574704 357490035 387135136 255645821 297849372 356499771 356576401 357493567 387135174 255647456 300078590 356499777 356577660 357497139 387135176 255648275 300669727 356499779 357114993 357497581 387135184 260279126 302142947 356501328 357115447 357497671 387135186 260279128 302142948 356502523 357115451 357500579 387135188 261343326 302142950 356503180 357115453 357504663 387135190 283132367 302142951 356503184 357116080 357504691 387135192 283362112 302765302 356503295 357116928 357504699 387135194 289188052 302796334 356504436 357117461 357504707 387135282 295841350 302811470 356504523 357117463 357505859 387135284 296088529 302821107 356504765 357117829 357510851 387135294 296090415 302821679 356511113 357117839 357516975 387135298 296090524 319759260 356515120 357125059 359477003 387135300 296090526 319759266 356517088 357126015 359477998 387135302 297599503 320148814 356520732 357134488 359478043 387135304 297601531 326489963 356522586 357135657 359478286 387135312 297611791 326490273 356522588 357138503 359484299 387135314 297722841 326491131 356522590 357139683 359486936 387135316 387135318 449440433 460376293 460413408 462423864 475546199 387135320 449445896 460378310 460416351 470101924 475556485 387135322 449446454 460380744 462394387 470102280 475559699 387135324 449447657 460381726 462394433 470102858 475578293 387135326 449449002 460382093 462394557 470104211 475591753 387135328 449449004 460382095 462395646 470104264 475593742 388493506 449449006 460382754 462395678 470104266 475612072 388495496 449451379 460384935 462396388 470106317 475622476 388498446 449451589 460384937 462396389 470106357 475622507 388499220 449451591 460385076 462396419 470115448 475623787 388502176 449451593 460385872 462396542 470130404 482550481 388517521 449453712 460386018 462397507 470131550 482550499 388519407 449453714 460389217 462399998 470136482 482550740 388521413 449453716 460394872 462400798 470136484 482550999 388827901 449453732 460396139 462401217 470136488 482552352 388827903 449457075 460397862 462402118 470136492 482554970 388827907 449467555 460397864 462402237 470137933 482555336 388827909 449468742 460398541 462402284 470137937 482555478 388827913 449495638 460403139 462402416 470140422 482556454 393887637 449495736 460403141 462404228 470140426 482557289 393887646 449499880 460403143 462406358 470140908 482558462 393887649 449502786 460403145 462408262 470141232 482558508 393990627 449503471 460405998 462409325 470142008 482558547 397746860 449503473 460407578 462409359 470142010 482561055 397789318 449515857 460407590 462409777 470142012 482561555 413924864 449518643 460409128 462411467 470143607 482562795 414590349 449519559 460409134 462414311 470143939 482562850 414590661 449522783 460409136 462414416 470145404 482565074 414591157 449524530 460409459 462414476 473923244 482566269 414879558 449524591 460409461 462415526 474114354 482566296 414879559 449528823 460409463 462415603 474143634 482566307 414879560 449528825 460409465 462415731 474202268 482568689 414888074 449534021 460409467 462416307 474299266 482570049 431812559 460365546 460410124 462416920 474363119 482570572 449432064 460366882 460410126 462416922 474366157 482575121 449432066 460369823 460410128 462416923 474429346 449433069 460369829 460410130 462416924 475432777 449436944 460369831 460410132 462417401 475473002 449438665 460369833 460410134 462419769 475489790 449438667 460370755 460410213 462420317 475511330 449440431 460374714 460411200 462423366 475516200

TABLE 1 GI number Accession Origin 190692175 ACE87855.1 Stevia rebaudiana 41469452 AAS07253.1 Oryza sativa 62857204 BAD95881.1 Ipomoea nil 62857206 BAD95882.1 Ipomoea purperea 56550539 BAD77944.1 Bellis perennis 115454819 NP_001051010.1 Oryza sativa Japonica Group 115459312 NP_001053256.1 Oryza sativa Japonica Group 115471069 NP_001059133.1 Oryza sativa Japonica Group 115471071 NP_001059134.1 Oryza sativa Japonica Group 116310985 CAH67920.1 Oryza sativa Indica Group 116788066 ABK24743.1 Picea sitchensis 122209731 Q2V6J9.1 Fragaria × ananassa 125534461 EAY81009.1 Oryza sativa Indica Group 125559566 EAZ05102.1 Oryza sativa Indica Group 125588307 EAZ28971.1 Oryza sativa Japonica Group 148907340 ABR16806.1 Picea sitchensis 148910082 ABR18123.1 Picea sitchensis 148910612 ABR18376.1 Picea sitchensis 15234195 NP_194486.1 Arabidopsis thaliana 15239523 NP_200210.1 Arabidopsis thaliana 15239937 NP_196793.1 Arabidopsis thaliana 1685005 AAB36653.1 Nicotiana tabacum 183013903 ACC38471.1 Medicago truncatula 186478321 NP_172511.3 Arabidopsis thaliana 187373030 ACD03249.1 Avena strigosa 194701936 ACF85052.1 Zea mays 19743740 AAL92461.1 Solanum lycopersicum 212275846 NP_001131009.1 Zea mays 222619587 EEE55719.1 Oryza sativa Japonica Group 224055535 XP_002298527.1 Populus trichocarpa 224101569 XP_002334266.1 Populus trichocarpa 224120552 XP_002318358.1 Populus trichocarpa 224121288 XP_002330790.1 Populus trichocarpa 225444853 XP_002281094 Vitis vinifera 225454342 XP_002275850.1 Vitis vinifera 225454475 XP_002280923.1 Vitis vinifera 225461556 XP_002285222 Vitis vinifera 225469540 XP_002270294.1 Vitis vinifera 226495389 NP_001148083.1 Zea mays 226502400 NP_001147674.1 Zea mays 238477377 ACR43489.1 Triticum aestivum 240254512 NP_565540.4 Arabidopsis thaliana 2501497 Q43716.1 Petunia × hybrida 255555369 XP_002518721.1 Ricinus communis 26452040 BAC43110.1 Arabidopsis thaliana 296088529 CBI37520.3 Vitis vinifera 297611791 NP_001067852.2 Oryza sativa Japonica Group 297795735 XP_002865752.1 Arabidopsis lyrata subsp. lyrata 297798502 XP_002867135.1 Arabidopsis lyrata subsp. lyrata 297820040 XP_002877903.1 Arabidopsis lyrata subsp. lyrata 297832276 XP_002884020.1 Arabidopsis lyrata subsp. lyrata 302821107 XP_002992218.1 Selaginella moellendorffii 30680413 NP_179446.2 Arabidopsis thaliana 319759266 ADV71369.1 Pueraria montana var. lobata 326507826 BAJ86656.1 Hordeum vulgare subsp. Vulgare 343457675 AEM37036.1 Brassica rapa subsp. oleifera 350534960 NP_001234680.1 Solanum lycopersicum 356501328 XP_003519477.1 Glycine max 356522586 XP_003529927.1 Glycine max 356535480 XP_003536273.1 Glycine max 357445733 XP_003593144.1 Medicago truncatula 357452783 XP_003596668.1 Medicago truncatula 357474493 XP_003607531.1 Medicago truncatula 357500579 XP_003620578.1 Medicago truncatula 357504691 XP_003622634.1 Medicago truncatula 359477998 XP_003632051.1 Vitis vinifera 359487055 XP_002271587 Vitis vinifera 359495869 XP_003635104.1 Vitis vinifera 387135134 AFJ52948.1 Linum usitatissimum 387135176 AFJ52969.1 Linum usitatissimum 387135192 AFJ52977.1 Linum usitatissimum 387135282 AFJ53022.1 Linum usitatissimum 387135302 AFJ53032.1 Linum usitatissimum 387135312 AFJ53037.1 Linum usitatissimum 388519407 AFK47765.1 Medicago truncatula 393887646 AFN26668.1 Barbarea vulgaris subsp. arcuata 414888074 DAA64088.1 Zea mays 42572855 NP974524.1 Arabidopsis thaliana 449440433 XP_004137989.1 Cucumis sativus 449446454 XP_004140986.1 Cucumis sativus 449449004 XP_004142255.1 Cucumis sativus 449451593 XP_004143546.1 Cucumis sativus 449515857 XP_004164964.1 Cucumis sativus 460382095 XP_004236775.1 Solanum lycopersicum 460409128 XP_004249992.1 Solanum lycopersicum 460409461 XP_004250157.1 Solanum lycopersicum 460409465 XP_004250159.1 Solanum lycopersicum 462396388 EMJ02187.1 Prunus persica 462402118 EMJ07675.1 Prunus persica 462409359 EMJ14693.1 Prunus persica 462416923 EMJ21660.1 Prunus persica 46806235 BAD17459.1 Oryza sativa Japonica Group 470104266 XP_004288529.1 Fragaria vesca subsp. vesca 470142008 XP_004306714.1 Fragaria vesca subsp. vesca 475432777 EMT01232.1 Aegilops tauschii 51090402 BAD35324.1 Oryza sativa Japonica Group

TABLE 2 GI number Accession Origin Internal reference 460409128 XP.004249992.1 Solanum lycopersicum UGTSL 460386018 XP.004238697.1 Solanum lycopersicum — 460409134 XP.004249995.1 Solanum lycopersicum — 460410132 XP.004250485.1 Solanum lycopersicum UGTSL2 460410130 XP.004250484.1 Solanum lycopersicum — 460410128 XP.004250483.1 Solanum lycopersicum — 460378310 XP.004234916.1 Solanum lycopersicum — 209954733 BAG80557.1 Lycium barbarum UGTLB 209954725 BAG80553.1 Lycium barbarum —

In yet another embodiment, the UDP-glucosyltransferase is any UDP-glucosyltransferase capable of adding at least one glucose unit to rebaudioside D to form rebaudioside M and/or rebaudioside M2. The UDP-glucosyltransferase may be, for example, UGT76G1. In preferred embodiments, conversion is at least greater than 50%, for example greater than 60%, greater than 70%, greater than 80% or greater than 90%.

The UGT76G1 enzyme may also contain on or more point mutations beneficial for conversion of rebaudioside D to rebaudioside M. Suitable mutations include, for example, S42A, F46I, I190L, S274G, I295M, K303G, F314S, K316R, K393R, V394I, I407V, N409K, N409R, Q425E, Q432E, S447A and S456L. In preferred embodiments, utilization of UGT76G1 containing such one or more point mutations results in increased rebaudioside M conversion of at least about 5% compared to use of the non-mutated UGT76G1 under the same conditions (wherein the results normalized). In preferred embodiments, conversion to rebaudioside M is increased from about 5% to about 50%, such as, for example, from about 10% to about 50%, from about 20% to about 50%, from about 30% to about 50% or about 40% to about 50%.

In some embodiments, a microorganism comprises an enzyme of the present invention, i.e. an enzyme capable of converting the organic compound to the target steviol glycoside. Accordingly, some embodiments of the present method include contacting a microorganism with a medium containing the starting composition to provide a medium comprising at least one target steviol glycoside.

The microorganism can be any microorganism possessing the necessary enzyme(s) for converting the organic compound to target steviol glycoside(s). These enzymes are encoded within the microorganism's genome.

Suitable microorganisms include, but are not limited to, E. coli, Saccharomyces sp., Aspergillus sp., Pichia sp., Bacillus sp., Yarrowia sp. etc.

In one embodiment, the microorganism is free when contacted with the starting composition.

In another embodiment, the microorganism is immobilized when contacted with the starting composition. For example, the microorganism may be immobilized to a solid support made from inorganic or organic materials. Non-limiting examples of solid supports suitable to immobilize the microorganism include derivatized cellulose or glass, ceramics, metal oxides or membranes. The microorganism may be immobilized to the solid support, for example, by covalent attachment, adsorption, cross-linking, entrapment or encapsulation.

In still another embodiment, the enzyme capable of converting the organic compound to the target steviol glycoside is secreted out of the microorganism and into the reaction medium.

The starting composition/organic compound is contacted with the biocatalyst or microorganism in an aqueous medium comprising water, and, e.g. various components selected from the including carbon sources, energy sources, nitrogen sources, microelements, vitamins, nucleosides, nucleoside phosphates, nucleoside diphosphates, nucleoside triphosphates, organic and inorganic salts, organic and mineral acids, bases etc. Carbon sources include glycerol, glucose, carbon dioxide, carbonates, bicarbonates. Nitrogen sources can include nitrates, nitrites, amino acids, peptides, peptones, or proteins.

In a particular embodiment, the medium comprises buffer. Suitable buffers include, but are not limited to, PIPES buffer, acetate buffer and phosphate buffer. In a particular embodiment, the medium comprises phosphate buffer.

In one embodiment, the medium can also include an organic solvent.

Optionally, the methods of the present invention further comprise recycling UDP to provide UDP-glucose. Accordingly, the methods comprise concomitantly recycling UDP by providing a recycling catalyst, i.e., a biocatalyst capable of UDP-glucose overproduction, and a recycling substrate, such that the conversion of the substrate steviol glycoside to the target steviol glycoside is carried out using catalytic amounts of UDP-glucosyltransferase and UDP-glucose (FIG. 2).

In one embodiment, the UDP-glucose recycling catalyst is sucrose synthase.

In one embodiment, the recycling substrate is sucrose.

The target steviol glycoside is optionally purified from the resulting composition. Purification of the target steviol glycoside from the reaction medium can be achieved by at least one suitable method to provide a highly purified target steviol glycoside composition. Suitable methods include crystallization, separation by membranes, centrifugation, extraction (liquid or solid phase), chromatographic separation, HPLC (preparative or analytical) or a combination of such methods.

In one embodiment, the present invention provides a method of producing stevioside by (a) contacting a medium containing a starting composition comprising rubusoside with UGT91D2 and UDP-glucose.

In a more particular embodiment, the present invention provides a catalytic method of producing stevioside by (a) contacting a medium containing a starting composition comprising rubusoside with a catalytic amount of UGT91D2 and UDP-glucose, and (b) recycling UDP-glucose by providing sucrose synthase and sucrose.

In another particular embodiment, the present invention provides a fermentation method of producing stevioside by (a) contacting a medium containing a starting composition comprising glucose with a microorganism comprising at least one enzyme capable of converting glucose to stevioside.

In still another particular embodiment, the present invention provides a fermentation method of producing stevioside by (a) contacting a medium containing a starting composition comprising glucose with a microorganism comprising at least one enzyme capable of converting glucose to stevioside and (b) recycling UDP-glucose by providing UDP-glucose, sucrose synthase and sucrose.

The methods above can further comprise purifying stevioside from the medium to provide a composition comprising highly purified stevioside.

In another embodiment, the present invention provides a method of producing rebaudioside E by (a) contacting a medium containing a starting composition comprising rubusoside with UGTSL2 and UDP-glucose.

In a more particular embodiment, the present invention provides a catalytic method of producing rebaudioside E by (a) contacting a medium containing a starting composition comprising rubusoside with a catalytic amount of UGTSL2 and UDP-glucose, and (b) recycling UDP-glucose by providing sucrose synthase and sucrose.

In another particular embodiment, the present invention provides a fermentation method of producing rebaudioside E by (a) contacting a medium containing a starting composition comprising glucose with a microorganism comprising at least one enzyme capable of converting glucose to rebaudioside E.

In still another particular embodiment, the present invention provides a fermentation method of producing rebaudioside E by (a) contacting a medium containing a starting composition comprising glucose with a microorganism comprising at least one enzyme capable of converting glucose to rebaudioside E and (b) recycling UDP-glucose by providing UDP-glucose, sucrose synthase and sucrose.

The methods above can further comprise purifying rebaudioside E from the medium to provide a composition comprising highly purified rebaudioside E.

In still another embodiment, the present invention provides a method of producing rebaudioside D by (a) contacting a medium containing a starting composition comprising rebaudioside E with UGT76G1 and UDP-glucose.

In a more particular embodiment, the present invention provides a catalytic method of producing rebaudioside D by (a) contacting a medium containing a starting composition comprising rebaudioside E with a catalytic amount of UGT76G1 and UDP-glucose, and (b) recycling UDP-glucose by providing sucrose synthase and sucrose.

In another particular embodiment, the present invention provides a fermentation method of producing rebaudioside D by (a) contacting a medium containing a starting composition comprising glucose with a microorganism comprising at least one enzyme capable of converting glucose to rebaudioside D.

In still another particular embodiment, the present invention provides a fermentation method of producing rebaudioside D by (a) contacting a medium containing a starting composition comprising glucose with a microorganism comprising at least one enzyme capable of converting glucose to rebaudioside D and (b) recycling UDP-glucose by providing UDP-glucose, sucrose synthase and sucrose.

The methods above can further comprise purifying rebaudioside D from the medium to provide a composition comprising highly purified rebaudioside D.

In yet another embodiment, the present invention provides a method of producing rebaudioside A by (a) contacting a medium containing a starting composition comprising stevioside with UGT76G1 and UDP-glucose.

In a more particular embodiment, the present invention provides a catalytic method of producing rebaudioside A by (a) contacting a medium containing a starting composition comprising stevioside with a catalytic amount of UGT76G1 and UDP-glucose, and (b) recycling UDP-glucose by providing sucrose synthase and sucrose.

In another particular embodiment, the present invention provides a fermentation method of producing rebaudioside A by (a) contacting a medium containing a starting composition comprising glucose with a microorganism comprising at least one enzyme capable of converting glucose to rebaudioside A.

In still another particular embodiment, the present invention provides a fermentation method of producing rebaudioside A by (a) contacting a medium containing a starting composition comprising glucose with a microorganism comprising at least one enzyme capable of converting glucose to rebaudioside A and (b) recycling UDP-glucose by providing UDP-glucose, sucrose synthase and sucrose.

The methods above can further comprise purifying rebaudioside A from the medium to provide a composition comprising highly purified rebaudioside A.

In a still further embodiment, the present invention provides a method of producing rebaudioside D, rebaudioside D2 and/or rebaudioside M2 by (a) contacting a medium containing a starting composition comprising rebaudioside A with UGT91D2, UGTSL2 or EUGT11 and UDP-glucose.

In a more particular embodiment, the present invention provides a catalytic method of producing rebaudioside D, rebaudioside D2 and/or rebaudioside M2 by (a) contacting a medium containing a starting composition comprising rebaudioside A with a catalytic amount of UGT91D2, UGTSL2 or EUGT11, and UDP-glucose, and (b) recycling UDP-glucose by providing sucrose synthase and sucrose.

In another particular embodiment, the present invention provides a fermentation method of producing rebaudioside D, rebaudioside D2 and/or rebaudioside M2 by (a) contacting a medium containing a starting composition comprising glucose with a microorganism comprising at least one enzyme capable of converting glucose to rebaudioside D, rebaudioside D2 and/or rebaudioside M2.

In still another particular embodiment, the present invention provides a fermentation method of producing rebaudioside D, rebaudioside D2 and/or rebaudioside M2 by (a) contacting a medium containing a starting composition comprising glucose with a microorganism comprising at least one enzyme capable of converting glucose to rebaudioside D, rebaudioside D2 and/or rebaudioside M2 and (b) recycling UDP-glucose by providing UDP-glucose, sucrose synthase and sucrose.

The methods above can further comprise separating rebaudioside D, rebaudioside D2 and/or rebaudioside M2 from the medium to provide a composition comprising highly purified rebaudioside D, rebaudioside D2 and/or rebaudioside M2.

In yet another embodiment, the present invention provides a method of producing rebaudioside M by (a) contacting a medium containing a starting composition comprising rebaudioside D with UGT76G1 and UDP-glucose.

In a more particular embodiment, the present invention provides a catalytic method of producing rebaudioside M by (a) contacting a medium containing a starting composition comprising rebaudioside D with a catalytic amount of UGT76G1 and UDP-glucose, and (b) recycling UDP-glucose by providing sucrose synthase and sucrose.

In another particular embodiment, the present invention provides a fermentation method of producing rebaudioside M by (a) contacting a medium containing a starting composition comprising glucose with a microorganism comprising at least one enzyme capable of converting glucose to rebaudioside M.

In still another particular embodiment, the present invention provides a fermentation method of producing rebaudioside M by (a) contacting a medium containing a starting composition comprising glucose with a microorganism comprising at least one enzyme capable of converting glucose to rebaudioside M and (b) recycling UDP-glucose by providing UDP-glucose, sucrose synthase and sucrose.

The methods above can further comprise separating rebaudioside M from the medium to provide a composition comprising highly purified rebaudioside M.

In some embodiment, multiple biocatalytic steps are performed sequentially to convert, e.g. (i) rebaudioside A to rebaudioside D, then (ii) rebaudioside D to rebaudioside M, or (i) stevioside to rebaudioside A, then (ii) rebaudioside A to rebaudioside D, then (iii) rebaudioside D to rebaudioside M, or (i) rubusoside to stevioside, then (ii) stevioside to rebaudioside A, then (iii) rebaudioside A to rebaudioside D, then (iv) rebaudioside D to rebaudioside M.

Alternatively, fermentation and biocatalytic steps can be used sequentially. For example, fermentation of a starting composition comprising glucose with a microorganism containing at least one enzyme capable of converting glucose to a target steviol glycoside can be performed first. The target steviol glycoside (which now becomes the starting material for the purposes of the next bioconversion) can then be contacted with a biocatalyst capable of converting it to the next target steviol glycoside.

Between each conversion the target steviol glycoside may optionally be separated from the medium prior to contacting the steviol glycoside (which now becomes the starting steviol glycoside for the purposes of the next bioconversion) with the next biocatalyst.

Compounds and Methods

The present invention also provides isolated and highly purified reb D2. Reb D2 is an isomer of reb D and has the following structure:

13-[(2-O-β-D-glucopyranosyl-3-O-β-D-glucopyranosyl-β-D-glucopyranosyl)oxy] ent-kaur-16-en-19-oic acid-[(6-O-β-D-glucopyranosyl-β-D-glucopyranosyl) ester]

In another embodiment, the present invention provides reb D2 having a purity greater than about 95% by weight on an anhydrous basis, such as, for example, greater than about 96% by weight, greater than about 97% by weight, greater than about 98% by weight or greater than about 99% by weight.

In still another embodiment, the present invention provides reb D2 having a purity greater than about 95% by weight in a steviol glycoside mixture, such as, for example, greater than about 96% by weight, greater than about 97% by weight, greater than about 98% by weight or greater than about 99% by weight.

The present invention also provides compositions comprising reb D2.

The present invention also provides a method for preparing reb D2 comprising:

    • a. contacting a starting composition comprising reb A with an enzyme capable of transforming reb A to reb D2, UDP-glucose, and optionally UDP-glucose recycling enzymes, to produce a composition comprising reb D2; and
    • b. isolating the composition comprising reb D2.

In some embodiments, the enzyme capable of transforming reb A to reb D2 is a UDP-glucosyltransferase, such as, for example, UGT91D2, UGTSL, UGTSL_Sc, UGTSL2 (GI No. 460410132 version XP_004250485.1), GI No. 460409128 (UGTSL) version XP_004249992.1, GI No. 115454819 version NP 001051010.1, GI No. 187373030, version ACD03249.1, GI No. 222619587 version EEE55719.1, GI No. 297795735 version XP_002865752.1 or EUGT11.

In one embodiment, the enzyme can be provided in the form of one or more cells containing said enzyme.

In other embodiments, the enzyme can be provided in the form of a whole cell suspension, a crude lysate, a purified enzyme or a combination thereof. In one embodiment, the enzyme is a purified enzyme. In another embodiment, the enzyme is provided in the form of a crude lysate. In still another embodiment, the enzyme is provided in the form of a whole cell suspension.

The enzyme capable of transforming reb A to reb D2 can be immobilized.

In another embodiment, the enzyme is provided in a microorganism.

In one embodiment, the microorganism is free when contacted with the starting composition.

In another embodiment, the microorganism is immobilized when contacted with the starting composition. For example, the microorganism may be immobilized to a solid support made from inorganic or organic materials. Non-limiting examples of solid supports suitable to immobilize the microorganism include derivatized cellulose or glass, ceramics, metal oxides or membranes. The microorganism may be immobilized to the solid support, for example, by covalent attachment, adsorption, cross-linking, entrapment or encapsulation.

Suitable microorganisms include, but are not limited to, E. coli, Saccharomyces sp., Aspergillus sp., Pichia sp., Bacillus sp., Yarrowia sp.

In still another embodiment, the enzyme is secreted out of the microorganism and into the reaction medium.

The starting composition is contacted with the enzyme or microorganism in an aqueous medium, comprising water, and various components selected from the group including carbon sources, energy sources, nitrogen sources, microelements, vitamins, nucleosides, nucleoside phosphates, nucleoside diphosphates, nucleoside triphosphates, organic and inorganic salts, organic and mineral acids, bases etc. Carbon sources include glycerol, glucose, carbon dioxide, carbonates, bicarbonates. Nitrogen sources can include nitrates, nitrites, amino acids, peptides, peptones, or proteins.

In a particular embodiment, the medium comprises buffer. Suitable buffers include, but are not limited to, PIPES buffer, acetate buffer and phosphate buffer. In a particular embodiment, the medium comprises phosphate buffer.

In one embodiment the medium can also include an organic solvent.

In a particular embodiment, the enzyme is a UDP-glucosyltransferase capable of transforming reb A to reb D2.

In a more particular embodiment, the enzyme is selected from UGT91D2, UGTSL, UGTSL_Sc, UGTSL2 (GI No. 460410132 version XP_004250485.1), GI No. 460409128 (UGTSL) version XP_004249992.1, GI No. 115454819 version NP_001051010.1, GI No. 187373030, version ACD03249.1, GI No. 222619587 version EEE55719.1, GI No. 297795735 version XP_002865752.1 or EUGT11 and UGTs having substantial (>85%) sequence identity to these enzymes.

In a still more particular embodiment, the enzyme is UGTSL2 or its improved variant produced by directed evolution and having higher activity.

In one embodiment, reb D2 is continuously removed from the medium while the conversion progresses. In yet another embodiment, reb D2 is separated and, optionally, purified from the reaction medium after completion of the reaction.

Isolation of reb D2 from the reaction medium can be achieved by any suitable method to provide a composition comprising reb D2. Suitable methods include, but are not limited to, lysis, crystallization, separation by membranes, centrifugation, extraction (liquid or solid phase), chromatographic separation, HPLC (preparative or analytical) or a combination of such methods. In a particular embodiment, isolation can be achieved by lysis and centrifugation.

In some embodiments, isolation may result in a reb D2 purity less than about 95% by weight on an anhydrous basis, and the composition may contain, e.g., steviol glycosides and/or residual reaction products. The composition comprising reb D2 can be further purified to provide highly purified reb D2, i.e. reb D2 having a purity greater than about 95% by weight on an anhydrous basis. In some embodiments, the compositions comprising reb D2 can be further purified to provide reb D2 having a purity greater than about 96%, greater than about 97%, greater than about 98% or greater than about 99% by weight on an anhydrous basis.

Purification can be affected by any means known to one of skill in the art including, but not limited to, crystallization, separation by membranes, centrifugation, extraction (liquid or solid phase), chromatographic separation, HPLC (preparative or analytical) or a combination of such methods. In a particular embodiment, HPLC is used to purify reb D2. In a more particular embodiment, semi-preparative HPLC is used to purify reb D2.

For example, a two-step semi-preparative HPLC purification can be used. The first step utilizes a C18 column with a mobile phase containing A (25% MeCN in water) and B (30% MeCN in water) with the following gradient:

Time (min) % A % B 0.0-5.0 100 0 20 20 80 25 20 80 30 100 0

The secondary step utilizes the same column and conditions, but with only an isocratic mobile phase: 20% MeCN in water.

Those of skill in the art will recognize that the particular column, mobile phases, injection volumes and other HPLC parameters can vary.

The present invention provides isolated and highly purified reb M2. Reb M2 is an isomer of reb M and has the following structure:

(13-[(2-O-β-D-glucopyranosyl-3-O-β-D-glucopyranosyl-β-D-glucopyranosyl)oxy] ent-kaur-16-en-19-oic acid-[(2-O-β-D-glucopyranosyl-6-O-β-D-glucopyranosyl-β-D-glucopyranosyl) ester])

In another embodiment, the present invention provides reb M2 having a purity greater than about 95% by weight on an anhydrous basis, such as, for example, greater than about 96% by weight, greater than about 97% by weight, greater than about 98% by weight or greater than about 99% by weight.

In still another embodiment, the present invention provides reb M2 having a purity greater than about 95% by weight in a steviol glycoside mixture, such as, for example, greater than about 96% by weight, greater than about 97% by weight, greater than about 98% by weight or greater than about 99% by weight.

In yet another embodiment, the present invention provides reb M2 having a purity greater than about 95% by weight in a stevia extract, such as, for example, greater than about 96% by weight, greater than about 97% by weight, greater than about 98% by weight or greater than about 99% by weight.

The present invention also provides compositions comprising reb M2.

It has been found that reb M2 is produced during biotransformation of reb A to reb D. As noted above, biotransformation of reb A to reb D also produces reb D2. Accordingly, the present invention also provides a method for preparing reb M2 comprising:

    • a. contacting a starting composition comprising reb A and/or reb D2 with an enzyme capable of transforming reb A and/or reb D2 to reb M2, UDP-glucose, and optionally UDP-glucose recycling enzymes to produce a composition comprising reb M2; and
    • b. isolating a composition comprising reb M2.

Not wishing to be bound by theory, it is currently believed that the pathway begins with transformation of reb A to reb D2, followed by transformation of reb D2 to reb M2. Accordingly, the present invention provides a method for preparing reb M2 comprising:

    • a. contacting a starting composition comprising reb D2 with an enzyme capable of transforming reb D2 to reb M2, UDP-glucose, and optionally UDP-glucose recycling enzymes to produce a composition comprising reb M2; and
    • b. isolating a composition comprising reb M2.

In yet another embodiment, a method for preparing reb M2 comprises:

    • a. contacting a starting composition comprising reb A with an enzyme capable of transforming reb A to reb D2, UDP-glucose, and optionally UDP-glucose recycling enzymes to produce a composition comprising reb D2;
    • b. optionally, isolating a composition comprising reb D2;
    • c. contacting the composition comprising reb D2 with an enzyme capable of transforming reb D2 to reb M2, UDP-glucose, and optionally UDP-glucose recycling enzymes to produce a composition comprising reb M2; and
    • d. isolating a composition comprising reb M2.

The enzyme can be a UDP-glucosyltransferase, such as, for example, UGT91D2, UGTSL, UGTSL_Sc, UGTSL2 (GI No. 460410132 version XP_004250485.1), GI No. 460409128 (UGTSL) version XP_004249992.1, GI No. 115454819 version NP_001051010.1, GI No. 187373030, version ACD03249.1, GI No. 222619587 version EEE55719.1, GI No. 297795735 version XP_002865752.1 or EUGT11.

In one embodiment, the enzyme can be provided in the form of one or more cells containing said enzyme.

In other embodiments, the enzyme can be provided in the form of a whole cell suspension, a crude lysate, a purified enzyme or a combination thereof. In one embodiment, the enzyme is a purified enzyme. In another embodiment, the enzyme is provided in the form of a crude lysate. In still another embodiment, the enzyme is provided in the form of a whole cell suspension.

In some embodiments, the enzyme can be immobilized.

In another embodiment, the enzyme is provided in a r microorganism.

In one embodiment, the microorganism is free when contacted with the starting composition.

In another embodiment, the microorganism is immobilized when contacted with the starting composition. For example, the microorganism may be immobilized to a solid support made from inorganic or organic materials. Non-limiting examples of solid supports suitable to immobilize the microorganism include derivatized cellulose or glass, ceramics, metal oxides or membranes. The microorganism may be immobilized to the solid support, for example, by covalent attachment, adsorption, cross-linking, entrapment or encapsulation.

Suitable microorganisms include, but are not limited to, E. coli, Saccharomyces sp., Aspergillus sp., Pichia sp., Bacillus sp., Yarrowia sp.

In still another embodiment, the enzyme is secreted out of the microorganism and into the reaction medium.

The starting composition is contacted with the enzyme or microorganism in aqueous medium, comprising water, and various components selected from the group including carbon sources, energy sources, nitrogen sources, microelements, vitamins, nucleosides, nucleoside phosphates, nucleoside diphosphates, nucleoside triphosphates, organic and inorganic salts, organic and mineral acids, bases etc. Carbon sources include glycerol, glucose, carbon dioxide, carbonates, bicarbonates. Nitrogen sources can include nitrates, nitrites, amino acids, peptides, peptones, or proteins.

In a particular embodiment, the medium comprises buffer. Suitable buffers include, but are not limited to, PIPES buffer, acetate buffer and phosphate buffer. In a particular embodiment, the medium comprises phosphate buffer.

In one embodiment the medium can also include an organic solvent.

In a particular embodiment, the enzyme is a UDP-glucosyltransferase capable of transforming reb A and/or reb D2 to reb M2 and is contained in E. coli.

In a more particular embodiment, the enzyme is selected from UGT91D2, UGTSL, UGTSL_Sc, UGTSL2 (GI No. 460410132 version XP_004250485.1), GI No. 460409128 (UGTSL) version XP_004249992.1, GI No. 115454819 version NP_001051010.1, GI No. 187373030, version ACD03249.1, GI No. 222619587 version EEE55719.1, GI No. 297795735 version XP_002865752.1 or EUGT11.

In a still more particular embodiment, the enzyme is UGTSL2 or its improved variant produced by directed evolution and having higher activity.

In one embodiment, reb M2 can be continuously removed from the medium while the conversion progresses. In yet another embodiment, reb M2 is separated, and optionally purified, from the reaction medium after the completion of the reaction.

Isolation of reb M2 from the reaction medium can be achieved by any suitable method to provide a composition comprising reb M2. Suitable methods include, but are not limited to, lysis, crystallization, separation by membranes, centrifugation, extraction (liquid or solid phase), chromatographic separation, HPLC (preparative or analytical) or a combination of such methods. In a particular embodiment, isolation can be achieved by lysis and centrifugation.

In some embodiments, isolation may result in a reb M2 purity less than about 95% by weight on an anhydrous basis, and the composition may contain, e.g., steviol glycosides and/or residual reaction products.

The composition comprising reb M2 can be further purified to provide highly purified reb M2, i.e. reb M2 having a purity greater than about 95% by weight on an anhydrous basis. In some embodiments, the compositions comprising reb M2 can be further purified to provide reb M2 having a purity greater than about 96%, greater than about 97%, greater than about 98% or greater than about 99% by weight on an anhydrous basis.

Purification can be affected by any means known to one of skill in the art including, but not limited to, crystallization, separation by membranes, centrifugation, extraction (liquid or solid phase), chromatographic separation, HPLC (preparative or analytical) or a combination of such methods. In a particular embodiment, HPLC is used to purify reb M2. In a more particular embodiment, semi-preparative HPLC is used to purify reb M2.

For example, a two-step semi-preparative HPLC purification can be used. The first step utilizes a C18 column with a mobile phase containing A (25% MeCN in water) and B (30% MeCN in water) with the following gradient:

Time (min) % A % B 0.0-5.0 100 0 20 20 80 25 20 80 30 100 0

The secondary step utilizes the same column and conditions, but with only an isocratic mobile phase: 20% MeCN in water.

Those of skill in the art will recognize that the particular column, mobile phases, injection volumes and other HPLC parameters can vary.

Purified steviol glycosides, prepared in accordance with the present invention, may be used in a variety of consumable products including, but not limited to, foods, beverages, pharmaceutical compositions, tobacco products, nutraceutical compositions, oral hygiene compositions, and cosmetic compositions.

The high purity reb M obtained in this invention, having a molecular weight of 1291.29, a molecular formula of C56H90O33, CAS registry number 1220616-44-3, and the structure presented in FIG. 1, is in the form of a white and odorless powder. The compound is about 200 times sweeter than sugar when compared to a 10% sucrose solution.

Other properties of the pure reb M compound include a melting point of 249-250° C., and a specific rotation of [α]D25−19.0° in 50% ethanol (C=1.0). The solubility of reb M in water is around 0.3%, and increases with an increase in temperature.

Reb M is soluble in diluted solutions of methanol, ethanol, n-propanol, and isopropanol. However, it is insoluble in acetone, benzene, chloroform, and ether.

Reb M obtained in accordance with the present invention is heat and pH-stable.

Highly purified target glycoside(s) particularly, reb D, reb D2, reb M and/or reb M2 obtained according to this invention can be used “as-is” or in combination with other sweeteners, flavors, food ingredients and combinations thereof.

Non-limiting examples of flavors include, but are not limited to, lime, lemon, orange, fruit, banana, grape, pear, pineapple, mango, berry, bitter almond, cola, cinnamon, sugar, cotton candy, vanilla and combinations thereof.

Non-limiting examples of other food ingredients include, but are not limited to, acidulants, organic and amino acids, coloring agents, bulking agents, modified starches, gums, texturizers, preservatives, antioxidants, emulsifiers, stabilizers, thickeners, gelling agents and combinations thereof.

Highly purified target glycoside(s) particularly, reb D, reb D2, reb M and/or reb M2 obtained according to this invention can be prepared in various polymorphic forms, including but not limited to hydrates, solvates, anhydrous, amorphous forms and combinations thereof.

Highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M and/or reb M2 obtained according to this invention may be incorporated as a high intensity natural sweetener in foodstuffs, beverages, pharmaceutical compositions, cosmetics, chewing gums, table top products, cereals, dairy products, toothpastes and other oral cavity compositions, etc.

Highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M and/or reb M2 as a sweetening compound may be employed as the sole sweetener, or it may be used together with one another or with at least one other naturally occurring high intensity sweeteners such as stevia, stevia extract, steviolmonoside, steviolbioside, stevioside, reb A, reb B, reb C, reb E, reb F, reb G, reb I, reb E, reb H, reb L, reb K, reb J, reb N, reb 0, steviolbioside, dulcoside A, dulcoside B, rubusoside, or other glycosides of steviol found in Stevia rebaudiana, mogrosides, brazzein, neohesperidin dihydrochalcone, glycyrrhizic acid and its salts, thaumatin, perillartine, pernandulcin, mukuroziosides, baiyunoside, phlomisoside-I, dimethyl-hexahydrofluorene-dicarboxylic acid, abrusosides, periandrin, carnosiflosides, cyclocarioside, pterocaryosides, polypodoside A, brazilin, hernandulcin, phillodulcin, glycyphyllin, phlorizin, trilobatin, dihydroflavonol, dihydroquercetin-3-acetate, neoastilibin, trans-cinnamaldehyde, monatin and its salts, selligueain A, hematoxylin, monellin, osladin, pterocaryoside A, pterocaryoside B, mabinlin, pentadin, miraculin, curculin, neoculin, chlorogenic acid, cynarin, Luo Han Guo sweetener, mogroside V, mogroside VI, grosmomomside, siamenoside, or other glycoside of mogrol found in Siraitia grosvenorii and combinations thereof.

In a particular embodiment, reb D2 and/or reb M2 can be used together in a sweetener composition comprising a compound selected from the group consisting of reb A, reb B, reb D, NSF-02, Mogroside V, Luo Han Guo, allulose, allose, D-tagatose, erythritol and combinations thereof.

Highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M and/or reb M2 may also be used in combination with synthetic high intensity sweeteners such as sucralose, potassium acesulfame, aspartame, alitame, saccharin, neohesperidin dihydrochalcone, cyclamate, neotame, dulcin, suosan advantame, salts thereof, and combinations thereof.

Moreover, highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M and/or reb M2 can be used in combination with natural sweetener suppressors such as gymnemic acid, hodulcin, ziziphin, lactisole, and others. Reb D, reb D2, reb M and/or reb M2 may also be combined with various umami taste enhancers. Reb D, reb D2, reb M and/or reb M2 can be mixed with umami tasting and sweet amino acids such as glutamate, aspartic acid, glycine, alanine, threonine, proline, serine, glutamate, lysine, tryptophan and combinations thereof.

Highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M can be used in combination with one or more additive selected from the group consisting of carbohydrates, polyols, amino acids and their corresponding salts, poly-amino acids and their corresponding salts, sugar acids and their corresponding salts, nucleotides, organic acids, inorganic acids, organic salts including organic acid salts and organic base salts, inorganic salts, bitter compounds, flavorants and flavoring ingredients, astringent compounds, proteins or protein hydrolysates, surfactants, emulsifiers, flavonoids, alcohols, polymers and combinations thereof.

Highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M and/or reb M2 may be combined with polyols or sugar alcohols. The term “polyol” refers to a molecule that contains more than one hydroxyl group. A polyol may be a diol, triol, or a tetraol which contain 2, 3, and 4 hydroxyl groups, respectively. A polyol also may contain more than four hydroxyl groups, such as a pentaol, hexaol, heptaol, or the like, which contain 5, 6, or 7 hydroxyl groups, respectively. Additionally, a polyol also may be a sugar alcohol, polyhydric alcohol, or polyalcohol which is a reduced form of carbohydrate, wherein the carbonyl group (aldehyde or ketone, reducing sugar) has been reduced to a primary or secondary hydroxyl group. Examples of polyols include, but are not limited to, erythritol, maltitol, mannitol, sorbitol, lactitol, xylitol, inositol, isomalt, propylene glycol, glycerol, threitol, galactitol, hydrogenated isomaltulose, reduced isomalto-oligosaccharides, reduced xylo-oligosaccharides, reduced gentio-oligosaccharides, reduced maltose syrup, reduced glucose syrup, hydrogenated starch hydrolyzates, polyglycitols and sugar alcohols or any other carbohydrates capable of being reduced which do not adversely affect the taste of the sweetener composition.

Highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M and/or reb M2 may be combined with reduced calorie sweeteners such as, for example, D-tagatose, L-sugars, L-sorbose, L-arabinose and combinations thereof.

Highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M and/or reb M2 may also be combined with various carbohydrates. The term “carbohydrate” generally refers to aldehyde or ketone compounds substituted with multiple hydroxyl groups, of the general formula (CH2O)n, wherein n is 3-30, as well as their oligomers and polymers. The carbohydrates of the present invention can, in addition, be substituted or deoxygenated at one or more positions. Carbohydrates, as used herein, encompass unmodified carbohydrates, carbohydrate derivatives, substituted carbohydrates, and modified carbohydrates. As used herein, the phrases “carbohydrate derivatives”, “substituted carbohydrate”, and “modified carbohydrates” are synonymous. Modified carbohydrate means any carbohydrate wherein at least one atom has been added, removed, or substituted, or combinations thereof. Thus, carbohydrate derivatives or substituted carbohydrates include substituted and unsubstituted monosaccharides, disaccharides, oligosaccharides, and polysaccharides. The carbohydrate derivatives or substituted carbohydrates optionally can be deoxygenated at any corresponding C-position, and/or substituted with one or more moieties such as hydrogen, halogen, haloalkyl, carboxyl, acyl, acyloxy, amino, amido, carboxyl derivatives, alkylamino, dialkylamino, arylamino, alkoxy, aryloxy, nitro, cyano, sulfo, mercapto, imino, sulfonyl, sulfenyl, sulfinyl, sulfamoyl, carboalkoxy, carboxamido, phosphonyl, phosphinyl, phosphoryl, phosphino, thioester, thioether, oximino, hydrazino, carbamyl, phospho, phosphonato, or any other viable functional group provided the carbohydrate derivative or substituted carbohydrate functions to improve the sweet taste of the sweetener composition.

Examples of carbohydrates which may be used in accordance with this invention include, but are not limited to, psicose, turanose, allose, tagatose, trehalose, galactose, rhamnose, various cyclodextrins, cyclic oligosaccharides, various types of maltodextrins, dextran, sucrose, glucose, ribulose, fructose, threose, arabinose, xylose, lyxose, allose, altrose, mannose, idose, lactose, maltose, invert sugar, isotrehalose, neotrehalose, isomaltulose, erythrose, deoxyribose, gulose, idose, talose, erythrulose, xylulose, psicose, turanose, cellobiose, amylopectin, glucosamine, mannosamine, fucose, glucuronic acid, gluconic acid, glucono-lactone, abequose, galactosamine, beet oligosaccharides, isomalto-oligosaccharides (isomaltose, isomaltotriose, panose and the like), xylo-oligosaccharides (xylotriose, xylobiose and the like), xylo-terminated oligosaccharides, gentio-oligosaccharides (gentiobiose, gentiotriose, gentiotetraose and the like), sorbose, nigero-oligosaccharides, palatinose oligosaccharides, fructooligosaccharides (kestose, nystose and the like), maltotetraol, maltotriol, malto-oligosaccharides (maltotriose, maltotetraose, maltopentaose, maltohexaose, maltoheptaose and the like), starch, inulin, inulo-oligosaccharides, lactulose, melibiose, raffinose, ribose, isomerized liquid sugars such as high fructose corn syrups, coupling sugars, and soybean oligosaccharides. Additionally, the carbohydrates as used herein may be in either the D- or L-configuration.

Highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M and/or reb M2 obtained according to this invention can be used in combination with various physiologically active substances or functional ingredients. Functional ingredients generally are classified into categories such as carotenoids, dietary fiber, fatty acids, saponins, antioxidants, nutraceuticals, flavonoids, isothiocyanates, phenols, plant sterols and stanols (phytosterols and phytostanols); polyols; prebiotics, probiotics; phytoestrogens; soy protein; sulfides/thiols; amino acids; proteins; vitamins; and minerals. Functional ingredients also may be classified based on their health benefits, such as cardiovascular, cholesterol-reducing, and anti-inflammatory. Exemplary functional ingredients are provided in WO2013/096420, the contents of which is hereby incorporated by reference.

Highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M and/or reb M2 obtained according to this invention may be applied as a high intensity sweetener to produce zero calorie, reduced calorie or diabetic beverages and food products with improved taste characteristics. It may also be used in drinks, foodstuffs, pharmaceuticals, and other products in which sugar cannot be used. In addition, highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M and/or reb M2 can be used as a sweetener not only for drinks, foodstuffs, and other products dedicated for human consumption, but also in animal feed and fodder with improved characteristics.

Examples of consumable products in which highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M and/or reb M2 may be used as a sweetening compound include, but are not limited to, alcoholic beverages such as vodka, wine, beer, liquor, and sake, etc.; natural juices; refreshing drinks; carbonated soft drinks; diet drinks; zero calorie drinks; reduced calorie drinks and foods; yogurt drinks; instant juices; instant coffee; powdered types of instant beverages; canned products; syrups; fermented soybean paste; soy sauce; vinegar; dressings; mayonnaise; ketchups; curry; soup; instant bouillon; powdered soy sauce; powdered vinegar; types of biscuits; rice biscuit; crackers; bread; chocolates; caramel; candy; chewing gum; jelly; pudding; preserved fruits and vegetables; fresh cream; jam; marmalade; flower paste; powdered milk; ice cream; sorbet; vegetables and fruits packed in bottles; canned and boiled beans; meat and foods boiled in sweetened sauce; agricultural vegetable food products; seafood; ham; sausage; fish ham; fish sausage; fish paste; deep fried fish products; dried seafood products; frozen food products; preserved seaweed; preserved meat; tobacco; medicinal products; and many others. In principle it can have unlimited applications.

During the manufacturing of products such as foodstuffs, drinks, pharmaceuticals, cosmetics, table top products, and chewing gum, the conventional methods such as mixing, kneading, dissolution, pickling, permeation, percolation, sprinkling, atomizing, infusing and other methods may be used.

Moreover, the highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M and/or reb M2 obtained in this invention may be used in dry or liquid forms. In one embodiment, a tabletop sweetener comprising reb D2 is provided. In another embodiment, a tabletop sweetener comprising reb M2 is provided.

The highly purified target steviol glycoside can be added before or after heat treatment of food products. The amount of the highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M and/or reb M2 depends on the purpose of usage. As discussed above, it can be added alone or in combination with other compounds.

The present invention is also directed to sweetness enhancement in beverages using reb D2 and/or reb M2. Accordingly, the present invention provides a beverage comprising a sweetener and reb D2 and/or reb M2 as a sweetness enhancer, wherein reb D2 and/or reb M2 is present in a concentration at or below their respective sweetness recognition thresholds.

As used herein, the term “sweetness enhancer” refers to a compound capable of enhancing or intensifying the perception of sweet taste in a composition, such as a beverage. The term “sweetness enhancer” is synonymous with the terms “sweet taste potentiator,” “sweetness potentiator,” “sweetness amplifier,” and “sweetness intensifier.”

The term “sweetness recognition threshold concentration,” as generally used herein, is the lowest known concentration of a sweet compound that is perceivable by the human sense of taste, typically around 1.0% sucrose equivalence (1.0% SE). Generally, the sweetness enhancers may enhance or potentiate the sweet taste of sweeteners without providing any noticeable sweet taste by themselves when present at or below the sweetness recognition threshold concentration of a given sweetness enhancer; however, the sweetness enhancers may themselves provide sweet taste at concentrations above their sweetness recognition threshold concentration. The sweetness recognition threshold concentration is specific for a particular enhancer and can vary based on the beverage matrix. The sweetness recognition threshold concentration can be easily determined by taste testing increasing concentrations of a given enhancer until greater than 1.0% sucrose equivalence in a given beverage matrix is detected. The concentration that provides about 1.0% sucrose equivalence is considered the sweetness recognition threshold.

In some embodiments, sweetener is present in the beverage in an amount from about 0.5% to about 12% by weight, such as, for example, about 1.0% by weight, about 1.5% by weight, about 2.0% by weight, about 2.5% by weight, about 3.0% by weight, about 3.5% by weight, about 4.0% by weight, about 4.5% by weight, about 5.0% by weight, about 5.5% by weight, about 6.0% by weight, about 6.5% by weight, about 7.0% by weight, about 7.5% by weight, about 8.0% by weight, about 8.5% by weight, about 9.0% by weight, about 9.5% by weight, about 10.0% by weight, about 10.5% by weight, about 11.0% by weight, about 11.5% by weight or about 12.0% by weight.

In a particular embodiment, the sweetener is present in the beverage in an amount from about 0.5% of about 10%, such as for example, from about 2% to about 8%, from about 3% to about 7% or from about 4% to about 6% by weight. In a particular embodiment, the sweetener is present in the beverage in an amount from about 0.5% to about 8% by weight. In another particular embodiment, the sweetener is present in the beverage in an amount from about 2% to about 8% by weight.

In one embodiment, the sweetener is a traditional caloric sweetener. Suitable sweeteners include, but are not limited to, sucrose, fructose, glucose, high fructose corn syrup and high fructose starch syrup.

In another embodiment, the sweetener is erythritol.

In still another embodiment, the sweetener is a rare sugar. Suitable rare sugars include, but are not limited to, D-allose, D-psicose, L-ribose, D-tagatose, L-glucose, L-fucose, L-arbinose, D-turanose, D-leucrose and combinations thereof.

It is contemplated that a sweetener can be used alone, or in combination with other sweeteners.

In one embodiment, the rare sugar is D-allose. In a more particular embodiment, D-allose is present in the beverage in an amount of about 0.5% to about 10% by weight, such as, for example, from about 2% to about 8%.

In another embodiment, the rare sugar is D-psicose. In a more particular embodiment, D-psicose is present in the beverage in an amount of about 0.5% to about 10% by weight, such as, for example, from about 2% to about 8%.

In still another embodiment, the rare sugar is D-ribose. In a more particular embodiment, D-ribose is present in the beverage in an amount of about 0.5% to about 10% by weight, such as, for example, from about 2% to about 8%.

In yet another embodiment, the rare sugar is D-tagatose. In a more particular embodiment, D-tagatose is present in the beverage in an amount of about 0.5% to about 10% by weight, such as, for example, from about 2% to about 8%.

In a further embodiment, the rare sugar is L-glucose. In a more particular embodiment, L-glucose is present in the beverage in an amount of about 0.5% to about 10% by weight, such as, for example, from about 2% to about 8%.

In one embodiment, the rare sugar is L-fucose. In a more particular embodiment, L-fucose is present in the beverage in an amount of about 0.5% to about 10% by weight, such as, for example, from about 2% to about 8%.

In another embodiment, the rare sugar is L-arabinose. In a more particular embodiment, L-arabinose is present in the beverage in an amount of about 0.5% to about 10% by weight, such as, for example, from about 2% to about 8%.

In yet another embodiment, the rare sugar is D-turanose. In a more particular embodiment, D-turanose is present in the beverage in an amount of about 0.5% to about 10% by weight, such as, for example, from about 2% to about 8%.

In yet another embodiment, the rare sugar is D-leucrose. In a more particular embodiment, D-leucrose is present in the beverage in an amount of about 0.5% to about 10% by weight, such as, for example, from about 2% to about 8%.

The addition of the sweetness enhancer at a concentration at or below its sweetness recognition threshold increases the detected sucrose equivalence of the beverage comprising the sweetener and the sweetness enhancer compared to a corresponding beverage in the absence of the sweetness enhancer. Moreover, sweetness can be increased by an amount more than the detectable sweetness of a solution containing the same concentration of the at least one sweetness enhancer in the absence of any sweetener.

Accordingly, the present invention also provides a method for enhancing the sweetness of a beverage comprising a sweetener comprising providing a beverage comprising a sweetener and adding a sweetness enhancer selected from reb D2, reb M2 or a combination thereof, wherein reb D2 and reb M2 are present in a concentration at or below their sweetness recognition thresholds.

Addition of reb D2 and/or reb M2 in a concentration at or below the sweetness recognition threshold to a beverage containing a sweetener may increase the detected sucrose equivalence from about 1.0% to about 5.0%, such as, for example, about 1.0%, about 1.5%, about 2.0%, about 2.5%, about 3.0%, about 3.5%, about 4.0%, about 4.5% or about 5.0%.

The following examples illustrate preferred embodiments of the invention for the preparation of highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M and/or reb M2. It will be understood that the invention is not limited to the materials, proportions, conditions and procedures set forth in the examples, which are only illustrative.

Example 1 In-Vivo Production of UGT76G1

NcoI and NdeI restriction sides were added to the original nucleic sequence as described in Genbank accession no. AAR06912.1. After codon optimization the following nucleic sequence was obtained:

(SEQ ID NO: 1) CCATGGCCCATATGGAAAACAAAACCGAAACCACCGTTCGTCGTCGTCGC CGTATTATTCTGTTTCCGGTTCCGTTTCAGGGTCATATTAATCCGATTCT GCAGCTGGCAAATGTGCTGTATAGCAAAGGTTTTAGCATTACCATTTTTC ATACCAATTTTAACAAACCGAAAACCAGCAATTATCCGCATTTTACCTTT CGCTTTATTCTGGATAATGATCCGCAGGATGAACGCATTAGCAATCTGCC GACACATGGTCCGCTGGCAGGTATGCGTATTCCGATTATTAACGAACATG GTGCAGATGAACTGCGTCGTGAACTGGAACTGCTGATGCTGGCAAGCGAA GAAGATGAAGAAGTTAGCTGTCTGATTACCGATGCACTGTGGTATTTTGC ACAGAGCGTTGCAGATAGCCTGAATCTGCGTCGTCTGGTTCTGATGACCA GCAGCCTGTTTAACTTTCATGCACATGTTAGCCTGCCGCAGTTTGATGAA CTGGGTTATCTGGATCCGGATGATAAAACCCGTCTGGAAGAACAGGCAAG CGGTTTTCCGATGCTGAAAGTGAAAGATATCAAAAGCGCCTATAGCAATT GGCAGATTCTGAAAGAAATTCTGGGCAAAATGATTAAACAGACCAAAGCA AGCAGCGGTGTTATTTGGAATAGCTTTAAAGAACTGGAAGAAAGCGAACT GGAAACCGTGATTCGTGAAATTCCGGCACCGAGCTTTCTGATTCCGCTGC CGAAACATCTGACCGCAAGCAGCAGCAGCCTGCTGGATCATGATCGTACC GTTTTTCAGTGGCTGGATCAGCAGCCTCCGAGCAGCGTTCTGTATGTTAG CTTTGGTAGCACCAGCGAAGTTGATGAAAAAGATTTTCTGGAAATTGCCC GTGGTCTGGTTGATAGCAAACAGAGCTTTCTGTGGGTTGTTCGTCCGGGT TTTGTTAAAGGTAGCACCTGGGTTGAACCGCTGCCGGATGGTTTTCTGGG TGAACGTGGTCGTATTGTTAAATGGGTTCCGCAGCAAGAAGTTCTGGCAC ACGGCGCAATTGGTGCATTTTGGACCCATAGCGGTTGGAATAGCACCCTG GAAAGCGTTTGTGAAGGTGTTCCGATGATTTTTAGCGATTTTGGTCTGGA TCAGCCGCTGAATGCACGTTATATGAGTGATGTTCTGAAAGTGGGTGTGT ATCTGGAAAATGGTTGGGAACGTGGTGAAATTGCAAATGCAATTCGTCGT GTTATGGTGGATGAAGAAGGTGAATATATTCGTCAGAATGCCCGTGTTCT GAAACAGAAAGCAGATGTTAGCCTGATGAAAGGTGGTAGCAGCTATGAAA GCCTGGAAAGTCTGGTTAGCTATATTAGCAGCCTGTAATAACTCGAG.

After synthesis of the gene and subcloning into pET30A+ vector using NdeI and XhoI cloning sites, the UGT76G1_pET30a+ plasmid was introduced in E. coli B121(DE3) and E. coli EC100 by electroporation. The obtained cells were grown in petri-dishes in the presence of Kanamycin and suitable colonies were selected and allowed to grow in liquid LB medium (erlenmeyer flasks). Glycerol was added to the suspension as cryoprotectant and 400 μL aliquots were stored at −20° C. and at −80° C.

The storage aliquots of E. coli BL21(DE3) containing the pET30A+_UGT76G1 plasmid were thawed and added to 30 mL of LBGKP medium (20 g/L Luria Broth Lennox; 50 mM PIPES buffer pH 7.00; 50 mM Phosphate buffer pH 7.00; 2.5 g/L glucose and 50 mg/L of Kanamycin). This culture was allowed to shake at 135 rpm at 30° C. for 8 h.

The production medium contained 60 g/L of overnight express instant TB medium (Novagen), 10 g/L of glycerol and 50 mg/L of Kanamycin. The medium was allowed to stir at 20° C. while taking samples to measure the OD and pH. The cultures gave significant growth and a good OD was obtained. After 40 h, the cells were harvested by centrifugation and frozen to yield 12.7 g of cell wet weight.

Lysis was performed by addition of Bugbuster Master mix (Novagen) and the lysate was recovered by centrifugation and kept frozen. Activity tests were performed with thawed lysate.

Example 2 In-Vitro Production of UGT76G1

The S30 T7 High Yield Protein expression system kit from Promega was used. 4 μg of UGT76G1_pET30a+ plasmid from E. coli EC100 was mixed with 80 μL of S30 premix plus and 72 μL of S30 T7 extract was added. Nuclease-free water was added in order to obtain a total volume of 200 μL and the resulting solution was incubated for 2 h at 30° C. 180 μL was used in the catalytic test reaction.

Example 3 In-Vitro Production of UGT91D2

NcoI and NdeI restriction sides were added to the original nucleic sequence as described in Genbank accession no. ACE87855.1. After codon optimization the following nucleic sequence was obtained:

(SEQ ID NO: 2) CCATGGCACATATGGCAACCAGCGATAGCATTGTTGATGATCGTAAACAG CTGCATGTTGCAACCTTTCCGTGGCTGGCATTTGGTCATATTCTGCCGTA TCTGCAGCTGAGCAAACTGATTGCAGAAAAAGGTCATAAAGTGAGCTTTC TGAGCACCACCCGTAATATTCAGCGTCTGAGCAGCCATATTAGTCCGCTG ATTAATGTTGTTCAGCTGACCCTGCCTCGTGTTCAAGAACTGCCGGAAGA TGCCGAAGCAACCACCGATGTTCATCCGGAAGATATTCCGTATCTGAAAA AAGCAAGTGATGGTCTGCAGCCGGAAGTTACCCGTTTTCTGGAACAGCAT AGTCCGGATTGGATCATCTATGATTATACCCATTATTGGCTGCCGAGCAT TGCAGCAAGCCTGGGTATTAGCCGTGCACATTTTAGCGTTACCACCCCGT GGGCAATTGCATATATGGGTCCGAGCGCAGATGCAATGATTAATGGTAGT GATGGTCGTACCACCGTTGAAGATCTGACCACCCCTCCGAAATGGTTTCC GTTTCCGACCAAAGTTTGTTGGCGTAAACATGATCTGGCACGTCTGGTTC CGTATAAAGCACCGGGTATTAGTGATGGTTATCGTATGGGTCTGGTTCTG AAAGGTAGCGATTGTCTGCTGAGCAAATGCTATCATGAATTTGGCACCCA GTGGCTGCCGCTGCTGGAAACCCTGCATCAGGTTCCGGTTGTTCCGGTGG GTCTGCTGCCTCCGGAAGTTCCGGGTGATGAAAAAGATGAAACCTGGGTT AGCATCAAAAAATGGCTGGATGGTAAACAGAAAGGTAGCGTGGTTTATGT TGCACTGGGTAGCGAAGTTCTGGTTAGCCAGACCGAAGTTGTTGAACTGG CACTGGGTCTGGAACTGAGCGGTCTGCCGTTTGTTTGGGCATATCGTAAA CCGAAAGGTCCGGCAAAAAGCGATAGCGTTGAACTGCCGGATGGTTTTGT TGAACGTACCCGTGATCGTGGTCTGGTTTGGACCAGCTGGGCACCTCAGC TGCGTATTCTGAGCCATGAAAGCGTTTGTGGTTTTCTGACCCATTGTGGT AGCGGTAGCATTGTGGAAGGTCTGATGTTTGGTCATCCGCTGATTATGCT GCCGATTTTTGGTGATCAGCCGCTGAATGCACGTCTGCTGGAAGATAAAC AGGTTGGTATTGAAATTCCGCGTAATGAAGAAGATGGTTGCCTGACCAAA GAAAGCGTTGCACGTAGCCTGCGTAGCGTTGTTGTTGAAAAAGAAGGCGA AATCTATAAAGCCAATGCACGTGAACTGAGCAAAATCTATAATGATACCA AAGTGGAAAAAGAATATGTGAGCCAGTTCGTGGATTATCTGGAAAAAAAC ACCCGTGCAGTTGCCATTGATCACGAAAGCTAATGACTCGAG

After synthesis of the gene and subcloning into pET30A+ vector using NcoI and XhoI cloning sites, the UGT91D2_pET30a+ plasmid was introduced into E. coli EC100 by electroporation. The obtained cells were grown in the presence of Kanamycin and suitable colonies were selected and allowed to grow in liquid LB medium (erlenmeyer flasks). Glycerol was added to the suspension as cryoprotectant and 400 μL aliquots were stored at −20° C. and at −80° C.

The S30 T7 High Yield Protein expression system kit from Promega was used for the in-vitro synthesis of the protein.

4 μg of UGT91D2_pET30a+ plasmid was mixed with 80 μL of S30 premix plus and 72 μL of S30 T7 extract was added. Nuclease-free water was added in order to obtain a total volume of 200 μL and the resulting solution was incubated for 2 h at 30° C. 5 μL was used for SDS-page analysis while the remaining 45 μL was used in the catalytic test reaction.

Example 4 Catalytic Reaction with In-Vivo Produced UGT76G1

The total volume of the reaction was 5.0 mL with the following composition: 50 mM sodium phosphate buffer pH 7.2, 3 mM MgCl2, 2.5 mM UDP-glucose, 0.5 mM Stevioside and 500 μL of UGT76G1 thawed lysate. The reactions were run at 30° C. on an orbitary shaker at 135 rpm. For each sample, 460 μL of the reaction mixture was quenched with 40 μL of 2N H2SO4 and 420 μL of methanol/water (6/4). The samples were immediately centrifuged and kept at 10° C. before analysis by HPLC (CAD). HPLC indicated almost complete conversion of stevioside to rebaudioside A (FIG. 4).

Example 5 Catalytic Reaction with In-Vitro Produced UGT91D2

The total volume of the reaction was 0.5 mL with the following composition: 50 mM sodium phosphate buffer pH 7.2, 3 mM MgCl2, 3.8 mM UDP-glucose, 0.1 mM Rebaudioside A and 180 μL of in-vitro produced UGT91D2. The reactions were run at 30° C. on an orbitary shaker at 135 rpm. For each sample, 450 μL of reaction mixture was quenched with 45 μL of 2N H2SO4 and 405 μL of 60% MeOH. After centrifugation, the supernatant was analyzed by HPLC (CAD). HPLC indicated a 4.7% conversion of rebaudioside A to rebaudioside D after 120 h.

Example 6 Catalytic Reaction with In-Vitro Produced UGT76G1

The total volume of the reaction was 2 mL with the following composition: 50 mM sodium phosphate buffer pH 7.2, 3 mM MgCl2, 3.8 mM UDP-glucose, 0.5 mM Rebaudioside D and 180 μL of in-vitro produced UGT76G1. The reactions were run at 30° C. on an orbitary shaker at 135 rpm. For each sample, 400 μL of reaction mixture was quenched with 40 μL of 2N H2SO4 and 360 μL of 60% MeOH. After centrifugation, the supernatant was analyzed by HPLC (CAD). HPLC indicated 80% conversion of rebaudioside D to rebaudioside M after 120 h (FIG. 5).

For examples 7 to 12, the following abbreviations are used:
LBGKP medium: 20 g/L Luria Broth Lennox; 50 mM PIPES buffer pH 7.00; 50 mM Phosphate buffer pH 7.00; 2.5 g/L glucose and 50 mg/L of Kanamycin or Ampicillin
LB medium: (20 g/L Luria Broth Lennox)

Example 7 Preparation and Activity of UGT76G1 Prepared by pET30a+Plasmid and BL21 (DE3) Expression Strain

The pET30a+_UGT76G1 plasmid was transformed into BL21(DE3) expression strain (Lucigen E. Cloni® EXPRESS Electrocompetent Cells). The obtained cells were grown on LB Agar medium in petri-dishes in the presence of Kanamycin. Suitable colonies were selected and allowed to grow in liquid LBGKP medium containing Kanamycin. Glycerol was added and 400 μL aliquots were stored at −20° C. and at −80° C.

A storage aliquot was thawed and added to 30 mL of LBGKP medium. This culture was allowed to shake at 30° C. for 8 h. and subsequently used to inoculate 400 mL of production medium containing 60 g/L of “Overnight express instant TB medium” (Novagen, reference 71491-5), 10 g/L of glycerol and 50 mg/L of Kanamycin. The medium was allowed to stir at 20° C. while taking samples to measure the OD (600 nm) and pH. After 40 h, the cells were harvested by centrifugation and frozen. The obtained cell wet weight was 10.58 g.

3.24 g of obtained pellet was lysed by addition of 8.1 mL of “Bugbuster Master mix” (Novagen, reference 71456) and 3.5 mL of water. The lysate was recovered by centrifugation and kept frozen.

Example 8 Preparation and Activity of UGT76G1 Prepared by pET30a+Plasmid and Tuner (DE3) Expression Strain

The pET30a+_UGT76G1 plasmid was transformed into Tuner (DE3) expression strain (Novagen Tuner™ (DE3) Competent cells) by heat shock treatment. The obtained cells were grown on LB Agar medium in petri-dishes in the presence of Kanamycin. Suitable colonies were selected and allowed to grow in liquid LBGKP medium containing Kanamycin). Glycerol was added and 400 μL aliquots were stored at −20° C. and at −80° C.

A storage aliquot was thawed and added to 100 mL of LB medium containing 50 mg/L of Kanamycin. This culture allowed to shake at 30° C. for 15 h. 4.4 mL of this culture was used to inoculate 200 mL of production medium containing LB. This medium was allowed to stir at 37° C. until an OD (600 nm) of 0.9 was obtained, after which 400 μL of a 100 mM IPTG solution was added and the medium was allowed to stir at 30° C. for 4 h. The cells were harvested by centrifugation and frozen. The obtained cell wet weight was 1.38 g.

The obtained pellet was lysed by addition of 4.9 mL of “Bugbuster Master mix” (Novagen, reference 71456) and 2.1 mL of water. The lysate was recovered by centrifugation and kept frozen.

Example 9 Preparation and Activity of UGT76G1 Prepared by pMAL Plasmid and BL21 Expression Strain

After subcloning the synthetic UGT76G1 gene into the pMAL plasmid using Nde1 and Sal1 cloning sites, the pMAL_UGT76G1 plasmid was transformed into BL21 expression strain (New England Biolabs BL21 Competent E. coli) by heat shock treatment. The obtained cells were grown on LB Agar medium in petri-dishes in the presence of Ampicillin. Suitable colonies were selected and allowed to grow in liquid LBGKP medium containing Ampicillin). Glycerol was added and 400 μL aliquots were stored at −20° C. and at −80° C.

A storage aliquot was thawed and added to 30 mL of LBGKP medium. This culture was allowed to shake at 30° C. for 8 h. and subsequently used to inoculate 400 mL of production medium containing 60 g/L of “Overnight express instant TB medium” (Novagen, reference 71491-5), 10 g/L of glycerol and 50 mg/L of Ampicillin. The medium was allowed to stir at 20° C. while taking samples to measure the OD and pH. After 40 h, the cells were harvested by centrifugation and frozen. The obtained cell wet weight was 5.86 g.

2.74 g of obtained pellet was lysed by addition of 9.6 mL of “Bugbuster Master Mix” (Novagen, reference 71456) and 4.1 mL of water. The lysate was recovered by centrifugation and kept frozen.

Example 10 Preparation and Activity of UGT76G1 Prepared by pMAL Plasmid and ArcticExpress Expression Strain

The pMAL_UGT76G1 plasmid was transformed into ArcticExpress expression strain (Agilent ArcticExpress competent cells) by heat shock treatment. The obtained cells were grown on LB Agar medium in petri-dishes in the presence of Ampicillin and Geneticin. Suitable colonies were selected and allowed to grow in liquid LBGKP medium containing of Ampicillin and Geneticin. Glycerol was added and 400 μL aliquots were stored at −20° C. and at −80° C.

A storage aliquot was thawed and added to 30 mL of LBGKP medium (containing Ampicillin and Geneticin). This culture was allowed to shake at 30° C. for 8 h. and subsequently used to inoculate 400 mL of production medium containing 60 g/L of “Overnight express instant TB medium” (Novagen, reference 71491-5), 10 g/L of glycerol and 50 mg/L of Ampicillin. The medium was allowed to stir at 12° C. while taking samples to measure the OD (600 nm) and pH. After 68 h, the cells were harvested by centrifugation and frozen. The obtained cell wet weight was 8.96 g.

2.47 g of the obtained pellet was lysed by addition of 8.73 mL of “Bugbuster Master Mix” (Novagen, reference 71456) and 3.79 mL of water. The lysate was recovered by centrifugation and kept frozen.

Example 11 Preparation and Activity of UGT76G1 Prepared by pCOLDIII Plasmid and ArcticExpress Expression Strain

After subcloning the synthetic UGT76G1 gene into the pCOLDIII plasmid using Nde1 and Xho1 cloning sites, the pCOLDIII_UGT76G1 plasmid was transformed into ArcticExpress expression strain (Agilent ArcticExpress competent cells) by heat shock treatment. The obtained cells were grown on LB Agar medium in petri-dishes in the presence of Ampicillin and Geneticin. Suitable colonies were selected and allowed to grow in liquid LBGKP medium containing Ampicillin and Geneticin. Glycerol was added and 400 μL aliquots were stored at −20° C. and at −80° C.

A storage aliquot was thawed and added to 30 mL of LBGKP medium (containing Ampicillin and Geneticin). This culture was allowed to shake at 30° C. for 8 h. and subsequently used to inoculate 400 mL of production medium containing 60 g/L of “Overnight express instant TB medium” (Novagen, reference 71491-5), 10 g/L of glycerol and 50 mg/L of Kanamycin. The medium was allowed to stir at 12° C. while taking samples to measure the OD (600 nm) and pH. After 63 h, the cells were harvested by centrifugation and frozen. The obtained cell wet weight was 6.54 g.

2.81 g of the obtained pellet was lysed by addition of 9.8 mL of “Bugbuster Master Mix” (Novagen, reference 71456) and 4.2 mL of water. The lysate was recovered by centrifugation and kept frozen.

Example 12 Preparation and Activity of UGT76G1 Prepared by pCOLDIII Plasmid and Origami2 (DE3) Expression Strain

The pCOLDIII_UGT76G1 plasmid was transformed into Origami2 (DE3) expression strain (Novagen Origami™2 (DE3) Competent Cells) by heat shock treatment. The obtained cells were grown on LB Agar medium in petri-dishes in the presence of Ampicillin. Suitable colonies were selected and allowed to grow in liquid LBGKP medium containing Ampicillin. Glycerol was added and 400 μL aliquots were stored at −20° C. and at −80° C.

A storage aliquot was thawed and added to 30 mL of LBGKP medium (containing Ampicillin). This culture was allowed to shake at 30° C. for 8 h. and subsequently used to inoculate 400 mL of production medium containing 60 g/L of “Overnight express instant TB medium” (Novagen, reference 71491-5), 10 g/L of glycerol and 50 mg/L of Kanamycin. The medium was allowed to stir at 12° C. while taking samples to measure the OD (600 nm) and pH. After 68 h, the cells were harvested by centrifugation and frozen. The obtained cell wet weight was 2.53 g.

1.71 g of the obtained pellet was lysed by addition of 6.0 mL of “Bugbuster Master mix” (Novagen, reference 71456) and 1.9 mL of water. The lysate was recovered by centrifugation and kept frozen.

Example 13 Determination of Activity

Activity tests were performed on a 5 mL scale with 500 μL of thawed lysate for the transformation of Stevioside to Rebaudioside A and Rebaudioside D to Rebaudioside M using 0.5 mM of substrate, 2.5 mM of UDP-Glucose and 3 mM MgCl2 in 50 mM Sodium Phosphate buffer at pH 7.2. Samples were taken and analyzed by HPLC. The results for the different preparations of UGT76G1 are summarized in the following table.

Transformation activity* Rebaudioside Stevioside to D to Expression Rebaudioside Rebaudioside Example Plasmid strain A M 7 pET30a+ BL21 (DE3) 29 U mL−1 0.31 U mL−1 8 pET30a+ Tuner (DE3) 33 U mL−1 0.40 U mL−1 9 pMAL BL21 20 U mL−1 0.15 U mL−1 10 pMAL ArticExpress 15 U mL−1 0.25 U mL−1 11 pCOLDIII ArticExpress 15 U mL−1 0.11 U mL−1 12 pCOLDIII Origami2 (DE3) 37 U mL−1 0.20 U mL−1 *Note The activities for the transformation of Stevioside and Rebaudioside M are mentioned per mL of lysate. 1 U will transform 1 μmol of substrate in 1 hour at 30° C. and pH 7.2

Example 14 50 mL Scale Reaction for the Transformation of Rebaudioside D to Rebaudioside M

5 mL of the lysate of Example 12 was used to transform Rebaudioside D to Rebaudioside M on a 50 mL scale. The reaction medium consisted of 50 mM Sodium Phosphate buffer pH 7.2, 3 mM of MgCl2, 2.5 mM of UDP-Glucose and 0.5 mM of Rebaudioside D. After allowing the reaction to be shaken at 30° C. for 90 h. 50 mL of ethanol was added and the resulting mixture was allowed to stir at −20° C. for 1 h. After centrifugation at 5000 g for 10 min. the supernatant was purified via ultrafiltration (Vivaflow MWCO 30000). 78 mL of permeate was obtained and the 9 mL of retentate was diluted with 9 mL of ethanol and resubjected to Ultrafiltration (Vivaflow MWCO 30000). Another 14 mL of filtrate was obtained, which was combined with the first permeate. The combined permeates were concentrated under reduced pressure at 30° C. until 32 mL of a clear solution was obtained.

The HPLC trace of the product mixture is shown in FIG. 3. HPLC was carried out on an Agilent 1200 series equipped with a binary pump, auto sampler, and thermostat column compartment. The method was isocratic, with a mobile phase composed of 70% water (0.1% formic acid): 30% acetonitrile. The flow rate was 0.1 μL/min. The column used was Phenomenex Prodigy 5μ ODS (3) 100 A; 250×2 mm. The column temperature was maintained at 40° C. The injection volume was 20-40 μl.

The material eluting at 31.325 minutes was isolated. Comparison with a known reb M standard via HPLC, 1H NMR and HRMS confirmed the material as reb M.

Example 15 Preparation of UGT91D2 Using pMAL Plasmid and BL21 Expression Strain

After subcloning the synthetic UGT91D2 gene into the pMAL plasmid using Nde1 and Sal1 cloning sites, the pMAL_UGT91D2 plasmid was transformed into BL21 expression strain (New England Biolabs BL21 Competent E. coli) by heat shock treatment. The obtained cells were grown on LB Agar medium in petri-dishes in the presence of Ampicillin. Suitable colonies were selected and allowed to grow in liquid LBGKP medium containing Ampicillin). Glycerol was added and 400 μL aliquots were stored at −20° C. and at −80° C.

A storage aliquot was thawed and added to 30 mL of LBGKP medium. This culture was allowed to shake at 30° C. for 8 h. and subsequently used to inoculate 400 mL of production medium containing 60 g/L of “Overnight express instant TB medium” (Novagen, reference 71491-5), 10 g/L of glycerol and 50 mg/L of Ampicillin. The medium was allowed to stir at 20° C. while taking samples to measure the OD and pH. After 40 h, the cells were harvested by centrifugation and frozen. The obtained cell wet weight is 12.32 g.

2.18 g of obtained pellet was lysed by addition of 7.7 mL of “Bugbuster Master Mix” (Novagen, reference 71456) and 3.2 mL of water. The lysate was recovered by centrifugation and used directly for activity testing.

Example 16 Preparation of UGT91D2 Using pMAL Plasmid and ArcticExpress Expression Strain

The pMAL_UGT91D2 plasmid was transformed into ArcticExpress expression strain (Agilent ArcticExpress competent cells) by heat shock treatment. The obtained cells were grown on LB Agar medium in petri-dishes in the presence of Ampicillin and Geneticin. Suitable colonies were selected and allowed to grow in liquid LBGKP medium containing Ampicillin and Geneticin. Glycerol was added and 400 μL aliquots were stored at −20° C. and at −80° C.

A storage aliquot was thawed and added to 30 mL of LBGKP medium (containing Ampicillin and Geneticin). This culture was allowed to shake at 30° C. for 8 h. and subsequently used to inoculate 400 mL of production medium containing 60 g/L of “Overnight express instant TB medium” (Novagen, reference 71491-5), 10 g/L of glycerol and 50 mg/L of Ampicillin. The medium was allowed to stir at 20° C. for 16 h. followed by another 50 h. at 12° C. while taking samples to measure the OD (600 nm) and pH. The cells were harvested by centrifugation and frozen. The obtained cell wet weight is 15.77 g.

2.57 g of the obtained pellet was lysed by addition of 9.0 mL of “Bugbuster Master Mix” (Novagen, reference 71456) and 3.8 mL of water. The lysate was recovered by centrifugation and used directly for activity testing.

Example 17 Preparation of UGT91D2 Using pET30a+Plasmid and Tuner (DE3) Expression Strain

The pET30a+_UGT91D2 plasmid was transformed into Tuner (DE3) expression strain (Novagen Tuner™ (DE3) Competent cells) by heat shock treatment. The obtained cells were grown on LB Agar medium in petri-dishes in the presence of Kanamycin. Suitable colonies were selected and allowed to grow in liquid LBGKP medium (containing Kanamycin). Glycerol was added and 400 μL aliquots were stored at −20° C. and at −80° C.

A storage aliquot was thawed and added to 100 mL of LB medium containing 50 mg/L of Kanamycin. This culture allowed to shake at 30° C. for 15 h. 6.2 mL of this culture was used to inoculate 500 mL of production medium containing LB. This medium was allowed to stir at 37° C. until an OD (600 nm) of 0.9 was obtained after which 500 μL of a 100 mM IPTG solution was added (IPTG concentration in medium is 100 μM) and the medium was allowed to stir at 30° C. for 4 h, the cells were harvested by centrifugation and frozen. The obtained cell wet weight is 4.02 g.

1.92 g of the obtained pellet was lysed by addition of 6.8 mL of “Bugbuster Master mix” (Novagen, reference 71456) and 2.8 mL of water. The lysate was recovered by centrifugation and tested directly for activity.

Example 18 Preparation of UGT91D2 Using pET30a+Plasmid and ArcticExpress Expression Strain

The pET30a+_UGT91D2 plasmid was transformed into ArcticExpress (DE3) expression strain (Agilent ArcticExpress competent cells) by heat shock treatment. The obtained cells were grown on LB Agar medium in petri-dishes in the presence of Kanamycin and Geneticin. Suitable colonies were selected and allowed to grow in liquid LBGKP medium containing of Kanamycin and Geneticin. Glycerol was added and 400 μL aliquots were stored at −20° C. and at −80° C.

A storage aliquot was thawed and added to 30 mL of LBGKP medium (containing Kanamycin and Geneticin). This culture was allowed to shake at 30° C. for 8 h. and subsequently used to inoculate 400 mL of production medium containing 60 g/L of “Overnight express instant TB medium” (Novagen, reference 71491-5), 10 g/L of glycerol and 50 mg/L of Ampicillin. The medium was allowed to stir at 20° C. for 16 h. followed by another 50 h. at 12° C. while taking samples to measure the OD (600 nm) and pH. After 60 h, the cells were harvested by centrifugation and frozen. The obtained cell wet weight is 16.07 g.

3.24 g of the obtained pellet was lysed by addition of 11.4 mL of “Bugbuster Master Mix” (Novagen, reference 71456) and 4.8 mL of water. The lysate was recovered by centrifugation and used directly for activity testing.

Example 19 Determination of Activity of In-Vivo Preparations of UGT91D2

Activity tests were performed at 5 mL scale with 1000 μL of lysate for the transformation of Rubusoside to Stevioside using 0.5 mM of substrate, 2.5 mM of UDP-Glucose and 3 mM MgCl2 in 50 mM Sodium Phosphate buffer at pH 7.2. Samples were taken and analyzed by HPLC. The results for the different preparations of UGT91D2 are summarized in the following table.

Transformation activity* Example Plasmid Expression strain Rubusoside to Stevioside 15 pMAL BL21  9 mU mL−1 16 pMAL ArcticExpress 60 mU mL−1 17 pET30a+ Tuner (DE3) 28 mU mL−1 18 pET30a+ ArcticExpress (DE3) 21 mU mL−1 *Note: The activities are mentioned per mL of lysate. 1 U will transform 1 μmol of substrate in 1 hour at 30° C. and pH 7.2

Example 20 Other Enzymes for Rebaudioside a to Rebaudioside D Conversion

The following genes of UDP-glucosyltransferases were identified from public databases, synthesized by DNA2.0 and subsequently subcloned in pET30a+ vector.

Conversion Microplate Position Gene Name Internal reference RebA to RebD C908201 A1 gi115454819_NP_001051010.1 S115N01 A1 Active C908201 G2 gi187373030_ACD03249.1 S115N01 G2 Active C908201 A7 gi460409128_XP_004249992.1 S115N05 A7 Active C912666 E1 gi222619587_EEE55719.1 S115N06 E1 Active C912666 C2 gi297795735_XP_002865752.1 S115N06 C2 Active

The aminoacid sequences are as follows:

>gi|115454819|ref|NP_001051010.1|Os03g0702500 [Oryza sativa Japonica Group] (SEQ ID NO: 3) MDDAHSSQSPLHVVIFPWLAFGHLLPCLDLAERLAARGHRVSFVSTPRNL ARLPPVRPELAELVDLVALPLPRVDGLPDGAEATSDVPFDKFELHRKAFD GLAAPFSAFLDTACAGGKRPDWVLADLMHHWVALASQERGVPCAMILPCS AAVVASSAPPTESSADQREAIVRSMGTAAPSFEAKRATEEFATEGASGVS IMTRYSLTLQRSKLVAMRSCPELEPGAFTILTRFYGKPVVPFGLLPPRPD GARGVSKNGKHDAIMQWLDAQPAKSVVYVALGSEAPMSADLLRELAHGLD LAGTRFLWAMRKPAGVDADSVLPAGFLGRTGERGLVTTRWAPQVSILAHA AVCAFLTHCGWGSVVEGLQFGHPLIMLPILGDQGPNARILEGRKLGVAVP RNDEDGSFDRGGVAGAVRAVVVEEEGKTFFANARKLQEIVADREREERCI DEFVQHLTSWNELKNNSDGQYP. >gi|187373030|gb|ACD03249.1|UDP-glycosyltrans- ferase [Avena strigosa] (SEQ ID NO: 4) MAVKDEQQSPLHILLFPFLAPGHLIPIADMAALFASRGVRCTILTTPVNA AIIRSAVDRANDAFRGSDCPAIDISVVPFPDVGLPPGVENGNALTSPADR LKFFQAVAELREPFDRFLADNHPDAVVSDSFFHWSTDAAAEHGVPRLGFL GSSMFAGSCNESTLHNNPLETAADDPDALVSLPGLPHRVELRRSQMMDPK KRPDHWALLESVNAADQKSFGEVFNSFHELEPDYVEHYQTTLGRRTWLVG PVALASKDMAGRGSTSARSPDADSCLRWLDTKQPGSVVYVSFGTLIRFSP AELHELARGLDLSGKNFVWVLGRAGPDSSEWMPQGFADLITPRGDRGFII RGWAPQMLILNHRALGGFVTHCGWNSTLESVSAGVPMVTWPRFADQFQNE KLIVEVLKVGVSIGAKDYGSGIENHDVIRGEVIAESIGKLMGSSEESDAI QRKAKDLGAEARSAVENGGSSYNDVGRLMDELMARRSSVKVGEDIIPTND GL. >gi|460409128|ref|XP_004249992.1|PREDICTED: cyanidin-3-O-glucoside 2-O-glucuronosyltrans- ferase-like [Solanum lycopersicum] (SEQ ID NO: 5) MSPKLHKELFFHSLYKKTRSNHTMATLKVLMFPFLAYGHISPYLNVAKKL ADRGFLIYFCSTPINLKSTIEKIPEKYADSIHLIELHLPELPQLPPHYHT TNGLPPNLNQVLQKALKMSKPNFSKILQNLKPDLVIYDILQRWAKHVANE QNIPAVKLLTSGAAVFSYFFNVLKKPGVEFPFPGIYLRKIEQVRLSEMMS KSDKEKELEDDDDDDDLLVDGNMQIMLMSTSRTIEAKYIDFCTALTNWKV VPVGPPVQDLITNDVDDMELIDWLGTKDENSTVFVSFGSEYFLSKEDMEE VAFALELSNVNFIWVARFPKGEERNLEDALPKGFLERIGERGRVLDKFAP QPRILNHPSTGGFISHCGWNSAMESIDFGVPIIAMPMHLDQPMNARLIVE LGVAVEIVRDDDGKIHRGEIAETLKGVITGKTGEKLRAKVRDISKNLKTI RDEEMDAAAEELIQLCRNGN. >gi|222619587|gb|EEE55719.1|hypothetical protein OsJ_04191 [Oryza sativa Japonica Group] (SEQ ID NO: 6) MHVVMLPWLAFGHILPFAEFAKRVARQGHRVTLFSTPRNTRRLIDVPPSL AGRIRVVDIPLPRVEHLPEHAEATIDLPSNDLRPYLRRAYDEAFSRELSR LLQETGPSRPDWVLADYAAYWAPAAASRHGVPCAFLSLFGAAALCFFGPA ETLQGRGPYAKTEPAHLTAVPEYVPFPTTVAFRGNEARELFKPSLIPDES GVSESYRFSQSIEGCQLVAVRSNQEFEPEWLELLGELYQKPVIPIGMFPP PPPQDVAGHEETLRWLDRQEPNSVVYAAFGSEVKLTAEQLQRIALGLEAS ELPFIWAFRAPPDAGDGDGLPGGFKERVNGRGVVCRGWVPQVKFLAHASV GGFLTHAGWNSIAEGLANGVRLVLLPLMFEQGLNARQLAEKKVAVEVARD EDDGSFAANDIVDALRRVMVGEEGDEFGVKVKELAKVFGDDEVNDRYVRD FLKCLSEYKMQRQG. >gi|297795735|ref|XP_002865752.1|UDP-glucoronosyl/ UDP-glucosyl transferase family protein [Arabidopsis lyrata subsp. lyrata] (SEQ ID NO: 7) MDDKKEEVMHIAMFPWLAMGHLLPFLRLSKLLAQKGHKISFISTPRNILR LPKLPSNLSSSITFVSFPLPSISGLPPSSESSMDVPYNKQQSLKAAFDLL QPPLTEFLRLSSPDWIIYDYASHWLPSIAKELGISKAFFSLFNAATLCFM GPSSSLIEESRSTPEDFTVVPPWVPFKSTIVFRYHEVSRYVEKTDEDVTG VSDSVRFGYTIDGSDAVFVRSCPEFEPEWFSLLQDLYRKPVFPIGFLPPV IEDDDDDTTWVRIKEWLDKQRVNSVVYVSLGTEASLRREELTELALGLEK SETPFFWVLRNEPQIPDGFEERVKGRGMVHVGWVPQVKILSHESVGGFLT HCGWNSVVEGIGFGKVPIFLPVLNEQGLNTRLLQGKGLGVEVLRDERDGS FGSDSVADSVRLVMIDDAGEEIREKVKLMKGLFGNMDENIRYVDELVGFM RNDESSQLKEEEEEDDCSDDQSSEVSSETDEKELNLDLKEEKRRISVYKS LSSEFDDYVANEKMG.

The tested plasmids were received in a microtiterplate containing a plasmid as freeze-dried solid in each separate well.

Suspension of Plasmids.

To each well was added 24 μL of ultra-pure sterile water and the microtiter plate was shaken for 30 minutes at Room Temperature. Subsequently, the plate was incubated at 4° C. for 1 hour. The content of each well were further mixed by pipetting up and down. The plasmid quantification was performed by Qubit2.0 analysis using 1 μL of suspension. Determined quantities of plasmids were:

Microtiter plate Position Internal reference [Plasmid] ng/μL C908201 A1 S115N01 A1 32.8 C908201 G2 S115N01 G2 41.0 C908201 A7 S115N05 A7 56.6 C912666 E1 S115N06 E1 64.0 C912666 C2 S115N06 C2 31.4

Transformation of Competent Cells with Plasmids.

Aliquots of chemically competent EC100 cells were taken from freezer at −80° C. and stored on ice. The cells were allowed to thaw on ice for 10 minutes. 10 μL of a dilution of above described plasmid solution was added to a sterile microtube of 1.5 mL (in order to transform each cell with 50 pg of DNA) and stored on ice. 100 μL of chemically competent cells was added to each microtube. After incubation of the chemically competent cells plasmid mixtures on ice for 20 min a thermal shock of 30 seconds at 42° C. was performed.

Further incubation was performed on ice for 2 minutes. To each microtube 300 μL of SOC medium was added and the resulting mixture was transferred to a sterile 15 mL tube. After incubate for 1 hour at 37° C. while shaking at 135 rpm, the mixture is spread on solid Luria Broth medium containing Kanamycin 50 μg/mL. The petri-dishes are allowed to incubate for 16 hours at 37° C.

Preparation of Stock Solutions in Glycerol and Purification of Plasmids.

To a 50 mL sterile Falcon Tube 10 mL of Luria Broth medium containing 50 μg/mL of Kanamycin was added. The medium was seeded with an isolated colony from the above described Petri dish and the cultures were allowed to incubate for 16 hours at 37° C. while shaking at 135 rpm.

To sterile microtube of 1.5 mL containing 300 μL of a 60% sterile glycerol solution, 600 μL of the culture was added. The stock solution was stored at −80° C.

The remainder of the culture was centrifuged at 5,525 g for 10 minutes at 10° C. and after removal of the supernatant, the pellet was stored on ice. The produced plasmids were purified according to the Qiagen Qiaprep Spin Miniprep kit (ref: 27106) and the plasmid yield was measured at 260 nm. The plasmid solution was stored at 4° C. Plasmid quantities were determined as follows:

Microtiter plate Position Internal reference of test [Plasmid] ng/μL C908201 A1 S115N01 A1 115.7 C908201 G2 S115N01 G2 120.4 C908201 A7 S115N05 A7 293.8 C912666 E1 S115N06 E1 126.1 C912666 C2 S115N06 C2 98.8

In-Vitro Expression of Enzymes.

18 μL of plasmid solution (containing approximately 1.5 μg of plasmid) was used for in-vitro expression according to the Promega S30 T7 High-Yield Protein Expression System (ref: L1110) kit. The expression medium was produced as follows:

S30 Premix Plus T7 S30 Extract Total Trials 30 μL 27 μL 57 μL reference 20 μL 18 μL 38 μL

The prepared expression medium mix was added to the plasmid solution and the solution was allowed to incubate at 30° C. for 3 hours while mixing the mixture every 45 minutes. 5 μL of the mixture was frozen whereas the remainder was used for the catalytic test for the conversion of Rebaudioside A to Rebaudioside D.

Catalytic Test for Transformation of Rebaudioside A to Rebaudioside D.

430 μL of a reaction mixture containing 0.5 mM Rebaudioside A, 3 mM MgCl2, 50 mM phosphate buffer (pH7.2) and 2.5 mM UDP-glucose was added to a 1.5 mL sterile microtube. 52 μL of the enzyme expression medium was added and the resulting mixture was allowed to react at 30° C. for 24 hours. 125 μL samples were taken after 2 hours, 16 hours and 24 hours and added to a 115 μL of 60% methanol and 10 μL of 2 N H2SO4. The quenched sample was centrifuged at 18,000 g for 2 minutes at RT. 200 μL was transferred to an HPLC vial and analyzed.

HPLC Analysis

The HPLC assay was performed as follows:

Apparatus

Equipment Supplier Reference Lot # Elite Hitachi L-2130 NA Photodiode Array Hitachi L-2455 NA Corona CAD detector ESA 70-6186A CO-2044 Injector 100 μL Hitachi NA Column Synergy 4u Hydro-RP Phenomenex 00G-4375-E0 588582-12 80A (250 × 4.60 mm)

Instrument Conditions

Column Temperature 55° C. Detection UV 205 nm; bw 400 nm CAD detection Analysis duration 15 min Injected volume 10 μL Flow rate  1 mL/min

Mobile Phase Gradient Program

% Water containing Time (min) 0.04% acetic acid % methanol 0 40 60 8 25 75 10 25 75 11 40 60 15 40 60

The enzyme S115N05 A7 had the highest activity for Reb A to Reb D conversion (ca. 22.4%). At least three enzymes produced a significant amount of an unknown glycoside (marked as Reb UNK; later identified as reb D2) along with reb D. An unknown peak at ˜4.5 min was later identified as reb M2.

The HPLC assay results are provided below:

Steviol glycoside conversion in reaction mixture (% area) Enzyme Reb D Reb UNK Reb A Internal (Retention (Retention (Retention reference Time ~5.8 min) Time ~6.7 min) Time ~9.1 min) S115N01 A1 2.1 ND 96.7 S115N01 G2 0.6 ND 99.4 S115N05 A7 22.4 23.3 46.7 S115N06 E1 0.14  7.0 92.8 S115N06 C2 0.28  3.9 95.8

Example 21 Activity of In-Vitro Produced EUGT11

EUGT11 gene, described in WO/2013/022989A2, was synthesized by DNA2.0 and subsequently subcloned in pET30a+ vector.

Conversion Internal RebA to Microplate Position GI number Version reference RebD C912666 G4 41469452 AAS07253.1 S115N08 G4 Active

The amino-acid sequence is as follows:

>gi|41469452|gb|AAS07253.1|putative UDP- glucoronosyl and UDP-glucosyl transferase [Oryza sativa Japonica Group] EUGT11 enzyme from patent application WO/2013/022989A2 (SEQ ID NO: 8) MHVVICPLLAFGHLLPCLDLAQRLACGHRVSFVSTPRNISRLPPVRPSLA PLVSFVALPLPRVEGLPNGAESTHNVPHDRPDMVELHLRAFDGLAAPFSE FLGTACADWVMPTSSAPRQTLSSNIHRNSSRPGTPAPSGRLLCPITPHSN TLERAAEKLVRSSRQNARARSLLAFTSPPLPYRDVFRSLLGLQMGRKQLN IAHETNGRRTGTLPLNLCRWMWKQRRCGKLRPSDVEFNTSRSNEAISPIG ASLVNLQSIQSPNPRAVLPIASSGVRAVFIGRARTSTPTPPHAKPARSAA PRAHRPPSSVMDSGYSSSYAAAAGMHVVICPWLAFGHLLPCLDLAQRLAS RGHRVSFVSTPRNISRLPPVRPALAPLVAFVALPLPRVEGLPDGAESTND VPHDRPDMVELHRRAFDGLAAPFSEFLGTACADWVIVDVFHHWAAAAALE HKVPCAMMLLGSAHMIASIADRRLERAETESPAAAGQGRPAAAPTFEVAR MKLIRTKGSSGMSLAERFSLTLSRSSLVVGRSCVEFEPETVPLLSTLRGK PITFLGLMPPLHEGRREDGEDATVRWLDAQPAKSVVYVALGSEVPLGVEK VHELALGLELAGTRFLWALRKPTGVSDADLLPAGFEERTRGRGVVATRWV PQMSILAHAAVGAFLTHCGWNSTIEGLMFGHPLIMLPIFGDQGPNARLIE AKNAGLQVARNDGDGSFDREGVAAAIRAVAVEEESSKVFQAKAKKLQEIV ADMACHERYIDGFIQQLRSYKD.

The tested plasmid was received in a microtiterplate containing a plasmid as freeze-dried solid in a separate well.

Suspension of Plasmid

To the well was added 24 μL of ultra-pure sterile water and the microtiter plate was shaken for 30 minutes at Room Temperature. Subsequently, the plate was incubated at 4° C. for 1 hour. The content of the well was further mixed by pipetting up and down. The plasmid quantification was performed by Qubit2.0 analysis using 1 μL of suspension. Plasmid quantity was determined as follows:

Microtiter plate Position Internal reference of test [Plasmid] ng/μL C912666 G4 S115N08 G4 19.2

Transformation of Competent Cells with Plasmid.

An aliquot of chemically competent EC100 cells was taken from freezer at −80° C. and stored on ice. The cells were allowed to thaw on ice for 10 minutes. 10 μL of a dilution of above described plasmid solution was added to a sterile microtube of 1.5 mL (in order to transform each cell with 50 pg of DNA) and stored on ice. 100 μL of chemically competent cells was added to the microtube. After incubation of the chemically competent cells/plasmid mixture on ice for 20 min a thermal shock of 30 seconds at 42° C. was performed.

Further incubation was performed on ice for 2 minutes. To the microtube 300 μL of SOC medium was added and the resulting mixture was transferred to a sterile 15 mL tube. After incubate for 1 hour at 37° C. while shaking at 135 rpm, the mixture is spread on solid Luria Broth medium containing Kanamycin 50 μg/mL. The Petri dish is allowed to incubate for 16 hours at 37° C.

Preparation of Stock Solutions in Glycerol and Purification of Plasmid.

To a 50 mL sterile Falcon Tube 10 mL of Luria Broth medium containing 50 μg/mL of Kanamycin was added. The medium was seeded with an isolated colony from the above described Petri dish and the cultures were allowed to incubate for 16 hours at 37° C. while shaking at 135 rpm.

To sterile microtube of 1.5 mL containing 300 μL of a 60% sterile glycerol solution, 600 μL of the culture was added. The stock solution was stored at −80° C.

The remainder of the culture was centrifuged at 5,525 g for 10 minutes at 10° C. and after removal of the supernatant, the pellet was stored on ice. The produced plasmids were purified according to the Qiagen Qiaprep Spin Miniprep kit (ref: 27106) and the plasmid yield was measured at 260 nm. The plasmid solution was stored at 4° C. Plasmid quantity was determined as follows:

Microtiter plate Position Internal reference of test [Plasmid] ng/μL C912666 G4 S115N08 G4 38.4

In-vitro Expression of EUGT11

18 μL of a diluted plasmid solution (containing approximately 1.5 μg of plasmid) was used for in-vitro expression according to the Promega S30 T7 High-Yield Protein Expression System (ref: L1110) kit. The expression medium was produced as follows:

S30 Premix Plus T7 S30 Extract DNA template Total Trials 30 μL 27 μL 18 μL (~1.5 μg) 75 μL reference 20 μL 18 μL 12 μL (~1.0 μg) 50 μL

The prepared expression medium mix was added to the plasmid solution and the solution was allowed to incubate at 30° C. for 3 hours while mixing the mixture every 45 minutes. 5 μL of the mixture was frozen whereas the remainder was used for the catalytic test for the conversion of Rebaudioside A to Rebaudioside D.

Catalytic Test for Transformation of Rebaudioside A to Rebaudioside D.

430 μL of a reaction mixture containing 0.5 mM Rebaudioside A, 3 mM MgCl2, 50 mM phosphate buffer (pH7.2) and 2.5 mM UDP-glucose was added to a 1.5 mL sterile microtube. 52 μL of the enzyme expression medium was added and the resulting mixture was allowed to react at 30° C. for 24 hours. 125 μL samples were taken after 2 hours, 16 hours and 24 hours and added to a 115 μL of 60% methanol and 10 μL of 2 N H2SO4. The quenched sample was centrifuged at 18,000 g for 2 minutes at RT. 200 μL was transferred to HPLC vial and analyzed.

HPLC Analysis.

The HPLC assay was performed as described in EXAMPLE 20.

The HPLC assay results are provided below:

Compound Retention time Integration (area) Rebaudioside D 5.797  54,654,810 Rebaudioside A 9.157 633,926,835 Total 688,581,645

Example 22 In-Vivo Production of Enzymes

The enzymes described in EXAMPLE 20 were produced in vivo.

The pET30A+ vector containing the gene corresponding to the enzyme was introduced in E. coli BL21(DE3) by heat shock. The obtained cells were grown in Petri dishes in the presence of Kanamycin and suitable colonies were selected and allowed to grow in liquid LB medium (Erlenmeyer flasks). Glycerol was added to the suspension as cryoprotector and 400 μL aliquots were stored at −20° C. and at −80° C.

The storage aliquots of E. coli BL21(DE3) containing the pET30A+_UGT plasmids were thawed and added to 30 mL of LBGKP medium (20 g/L Luria Broth Lennox; 50 mM PIPES buffer pH 7.00; 50 mM Phosphate buffer pH 7.00; 2.5 g/L glucose and 50 mg/L of Kanamycine). This culture was allowed to shake at 135 rpm at 30° C. for 8 hrs.

The production medium contained 60 g/L of overnight express instant TB medium (Novagen), 10 g/L of glycerol and 50 mg/L of Kanamycine. The preculture was added to 400 mL of this medium and the solution was allowed to stir at 20° C. while taking samples to measure the OD and pH. The cultures gave significant growth and a good OD was obtained. After 40 hrs, the cells were harvested by centrifugation and frozen. The following yields of cell wet weights (CWW) are mentioned below.

GI number Version CWW 115454819 NP_001051010.1 9.2 g 187373030 ACD03249.1 7.4 g 460409128 XP_004249992.1 6.8 g 222619587 EEE55719.1 7.5 g 297795735 XP_002865752.1 8.8 g

Lysis was performed by addition of Bugbuster Master mix (Novagen) and the lysate was recovered by centrifugation and used fresh.

Determination of Activity.

Activity tests were performed at 5 mL scale with 1,000 μL of thawed lysate for the transformation of Rebaudioside A using 0.5 mM of substrate, 2.5 mM of UDP-Glucose and 3 mM MgCl2 in 50 mM Sodium Phosphate buffer at pH 7.2. Samples were taken and analyzed by HPLC.

HPLC Analysis.

The HPLC assay was performed as described in EXAMPLE 20.

The results for the different enzymes are provided below.

GI Number Version Conversion after 45 hrs. Reb D selectivity 115454819 NP_001051010.1  1.1%  100% 187373030 ACD03249.1  0.8%  100% 460409128 XP_004249992.1 62.1% 43.6% 222619587 EEE55719.1  2.9% Reb D Not detected 297795735 XP_002865752.1  0.0% Reb D Not detected

HPLC analysis also showed two unknown peaks. The peak at ˜4.5 min was later identified as reb M2. The peak at ˜7.6 min was later identified as reb D2.

Example 23 Identification of Glycosides

The reaction mixtures representing GI No. 460409128 of EXAMPLE 20 (hereinafter S115N05A7) and t EXAMPLE 22 (hereinafter S129N04) were additionally assayed by LC-MS to identify the unknown glycosides. An Agilent 1200 series HPLC system, equipped with binary pump (G1312B), autosampler (G1367D), thermostatted column compartment (G1316B), DAD detector (G1315C), connected with Agilent 6110A MSD, and interfaced with “LC/MSD Chemstation” software, was used.

Instrument Conditions

Column Phenomenex Kinetex 2.6u C18 100A, 4.6 mm × 150 mm, 2.6 μm Column Temperature 55° C. Detection DAD at 210 nm bw 360 nm MSD (Scan and SIM mode) Mode: ES-API, Negative Polarity Drying gas flow: 13.0 L/min Nebulizer pressure: 30 psig Drying gas temperature: 270° C. Analysis duration 25 min Injected volume  2 μL Flow rate  1 mL/min

Mobile Phase Gradient Program

Time (min) A (%): Formic acid 0.1% B (%): Acetonitrile 0 75 25 8.5 75 25 10.0 71 29 16.5 70 30

The compound observed on LCMS system at 3.5 min, corresponds to the unknown peak at ˜4.5 min in EXAMPLES 20 and 22. The LCMS data suggests that this compound has six glucosidic residues (C56H90O33) in its structure, and was found to be an isomer form of reb M, namely reb M2 (see Example 40 for discussion).

The compound observed on LCMS system at 7.6 min, corresponds to the unknown peak at ˜7.6 min in EXAMPLES 20 and 22. The LCMS data suggests that this compound has five glucosidic residues (C50H80O28) in its structure, and was found to be an isomer form of reb D, namely reb D2 (see Example 39 for discussion). The ratio of these compounds are provided below.

Steviol glycoside conversion in reaction mixture (% area) Sample Unknown@RT3.5 Reb D Unknown@RT7.6 Reb A S115N05A7 6.47 20.35 19.93 53.24 S129N04 6.05 23.73 21.22 49.00

Example 24 Identification of Glycosides

The reaction mixture representing GI No. 460409128 of EXAMPLE 22 (hereinafter S129N04) were additionally assayed by LC-MS along with Stevia rebaudiana Bertoni leaf extract “MLD1” produced by PureCircle Sdn Bhd (Malaysia) to determine the occurrence of S129N04 glycosides in nature.

The assay showed that the compound observed on LCMS system at 3.5 min, in EXAMPLE 23 (C56H90O33; later confirmed as reb M2), and the compound observed on LCMS system at 7.6 min, in EXAMPLE 23 (C50H80O28; reb UNK; later confirmed as reb D2) occur in the extract of Stevia rebaudiana Bertoni plant.

Example 25 Conversion of Rebaudioside E to Rebaudioside D

The total volume of the reaction was 5.0 mL with the following composition: 100 mM potassium phosphate buffer pH 7.5, 3 mM MgCl2, 2.5 mM UDP-glucose, 0.5 mM Rebaudioside E and 500 μL of UGT76G1 thawed lysate UGT76G1 gene was cloned in pET30a+ vector and expressed in E. coli BL21 (DE3)). The reactions were run at 30° C. on an orbitary shaker at 135 rpm. For sampling 300 μL of the reaction mixture was quenched with 30 μL of 2N H2SO4 and 270 μL of methanol/water (6/4). The samples were immediately centrifuged and kept at 10° C. before analysis by HPLC (CAD detection). The following reaction profile was obtained corresponding to a complete conversion of Rebaudioside E to Rebaudioside D.

Example 26 Directed Evolution of UGT76G1 for the Conversion of Rebaudioside D to Rebaudioside M

Starting from the amino acid sequence of UGT76G1, as is described in Genbank (AAR06912.1), different mutations at various amino acid positions were identified that could alter the activity of the enzyme for the transformation of Rebaudioside D (Reb D) to Rebaudioside M (Reb M). This list of mutations, designed by DNA2.0 ProteinGPS™ strategy, was subsequently used to synthesize 96 variant genes that contained 3, 4 or 5 of these mutations that were codon-optimized for expression in E. coli. The genes were subcloned in the pET30a+ plasmid and used for transformation of E. coli BL21 (DE3) chemically competent cells. The obtained cells were grown in Petri-dishes on solid LB medium in the presence of Kanamycin. Suitable colonies were selected and allowed to grow in liquid LB medium in tubes. Glycerol was added to the suspension as cryoprotectant and 400 μL aliquots were stored at −20° C. and at −80° C.

These storage aliquots of E. coli BL21(DE3) containing the pET30a+_UGT76G1var plasmids were thawed and added to LBGKP medium (20 g/L Luria Broth Lennox; 50 mM PIPES buffer pH 7.00; 50 mM Phosphate buffer pH 7.00; 2.5 g/L glucose and 50 mg/L of Kanamycine). This culture was allowed to shake in a 96 microtiter plate at 135 rpm at 30° C. for 8 h.

3.95 mL of production medium containing 60 g/L of Overnight Express™ Instant TB medium (Novagen®), 10 g/L of glycerol and 50 mg/L of Kanamycin was inoculated with 50 μL of above described culture. In a 48 deepwell plate the resulting culture was allowed to stir at 20° C. The cultures gave significant growth and a good OD (600 nm; 1 cm) was obtained. After 44 h, the cells were harvested by centrifugation and frozen.

Lysis was performed by addition of Bugbuster® Master mix (Novagen®) to the thawed cells and the lysate was recovered by centrifugation. Activity tests were performed with 100 μL of fresh lysate that was added to a solution of Rebaudioside D (final concentration 0.5 mM), MgCl2 (final concentration 3 mM) and UDP-Glucose (final concentration 2.5 mM) in 50 mM phosphate buffer pH 7.2.

The reaction was allowed to run at 30° C. and samples were taken after 2, 4, 7 and 24 h. to determine conversion and initial rate by HPLC (CAD detection) using the analytical method that was described above for the transformation of Rebaudioside D to Rebaudioside M. The results are depicted in the following table.

conversion Reb D initial rate Clone Mutations* to Reb M after 24 h (%) (Reb M area/min) UGT76G1var1 E224A_F314S_R334K 51.8   5.5E+07 UGT76G1var2 S274G_T284I_L379G 49.3   4.7E+07 UGT76G1var3 I295T_S357C_V366I 9.6   1.6E+06 UGT76G1var4 E224D_E231A_F265I 14.7   8.6E+06 UGT76G1var5 F22Y_I373L_P382M 3.5   2.3E+06 UGT76G1var6 Q266S_S357N_I373L 0.5   1.8E+06 UGT76G1var7 F22L_I43V_A239V 0.2 −6.0E+04 UGT76G1var8 E224A_Q266S_Q342E 0.5   2.3E+04 UGT76G1var9 E231A_D301N_G348P 52.0   4.9E+07 UGT76G1var10 A33G_L246F_Q342E 0.3 −7.7E+02 UGT76G1var11 F22L_A33G_V310I 0.4   3.8E+04 UGT76G1var12 L243P_K303G_A352G 0.5   8.7E+04 UGT76G1var13 L243A_S357C_A385T 0.2 −3.3E+04 UGT76G1var14 A239I_F265I_V396F 5.3   1.5E+06 UGT76G1var15 F41L_L246F_Q425E 5.6   1.5E+06 UGT76G1var16 F265I_P272A_I335V 18.6   5.8E+06 UGT76G1var17 F265L_Q266E_Q342K 0.7   7.2E+05 UGT76G1var18 L243P_S274G_N409R 1.9   5.0E+05 UGT76G1var19 E224D_E229A_Q432E 10.5   5.5E+06 UGT76G1var20 S375M_K393G_Y397E 1.8   1.9E+06 UGT76G1var21 A239V_V300A_K303G 41.9   3.3E+07 UGT76G1var22 E231A_V310I_R334K 34.4   2.4E+07 UGT76G1var23 T263S_G348P_A352G 47.8   4.1E+07 UGT76G1var24 A239I_P272A_Q425E 31.0   2.1E+07 UGT76G1var25 T284L_Q342K_Y397Q 0.9   6.3E+04 UGT76G1var26 S241I_F265L_F377C 1.8   7.5E+05 UGT76G1var27 A239I_L379A_V394I 29.0   1.5E+07 UGT76G1var28 L243A_S274G_P382M 6.1   2.4E+06 UGT76G1var29 F22Y_V279I_N409R 41.0   2.9E+07 UGT76G1var30 I43V_E224A_S241I 13.6   5.6E+06 UGT76G1var31 E224D_L243P_V300A 0.4   2.4E+05 UGT76G1var32 A239V_L243A_S375M 0.0 −4.4E+04 UGT76G1var33 A33G_R334H_Y397Q 1.0   7.5E+06 UGT76G1var34 I43V_T284I_I295T 3.4   1.5E+06 UGT76G1var35 T284L_F314S_S357N 0.5   1.8E+05 UGT76G1var36 F265L_L379A_V396F 20.0   8.8E+06 UGT76G1var37 E229A_L379G_I407V 39.1   2.8E+07 UGT76G1var38 F41L_I295M_F377C 8.2   3.7E+06 UGT76G1var39 F22Y_F41L_V366I 7.2   3.3E+06 UGT76G1var40 T263 S_Q266E_S375R 47.6   3.3E+07 UGT76G1var41 L246F_A385T_K393G 0.8   1.4E+06 UGT76G1var42 T263S_Q266S_R334H 34.6   2.2E+07 UGT76G1var43 S241I_P272A_V279I 19.9   9.4E+06 UGT76G1var44 I335V_S375R_I407V 35.3   2.3E+07 UGT76G1var45 V279I_D301N_S389E 38.6   2.3E+07 UGT76G1var46 F22L_Q266E_I295M 0.6   9.8E+05 UGT76G1var47 E229A_T284I_S389E 4.8   2.7E+06 UGT76G1var48 V394I_Y397E_Q432E 47.6   3.8E+07 UGT76G1var49 F41L_Q266E_T284I_Y397Q 2.6   1.1E+06 UGT76G1var50 F22Y_V310I_S375M_F377C 1.9   7.9E+05 UGT76G1var51 K303G_S357C_S389E_V396F 18.7   9.5E+06 UGT76G1var52 D301N_I373L_F377C_I407V 12.9   4.6E+06 UGT76G1var53 R334K_A352G_P382M_S389E 9.3   4.1E+06 UGT76G1var54 E229A_T284L_R334K_Q342E 0.7   4.3E+05 UGT76G1var55 I295M_Q342E_V366I_N409R 1.0   2.2E+05 UGT76G1var56 L246F_A352G_S357N_Q432E 0.4   4.1E+04 UGT76G1var57 S241I_T263S_L379G_A385T 0.8   1.5E+05 UGT76G1var58 S357C_S375M_N409R_Q425E 7.5   2.2E+06 UGT76G1var59 I335V_K393G_V394I_Y397Q 33.0   2.7E+07 UGT76G1var60 E231A_L243A_V279I_S357N 0.5   9.5E+04 UGT76G1var61 I43V_F265I_Q266S_L379A 6.4   2.0E+06 UGT76G1var62 L243P_P272A_V394I_V396F 0.1   3.4E+04 UGT76G1var63 F314S_R334H_Q342K_L379G 3.4   1.2E+06 UGT76G1var64 F22L_A239I_R334H_I407V 0.3   3.1E+04 UGT76G1var65 A33G_A239V_P382M_Q425E 1.2   3.3E+05 UGT76G1var66 F265L_V310I_V366I_A385T 0.8   3.7E+05 UGT76G1var67 E224D_F314S_S375R_Y397E −2.1 −5.6E+05 UGT76G1var68 Q342K_G348P_I373L_Y397E −1.4 −1.1E+05 UGT76G1var69 S274G_I295T_I335V_L379A 24.7   8.3E+06 UGT76G1var70 E224A_I295T_V300A_G348P 24.0   8.4E+06 UGT76G1var71 I295M_V300A_K393G_Q432E 42.9   2.1E+07 UGT76G1var72 T284L_D301N_K303G_S375R 19.2   9.1E+06 UGT76G1var73 F22Y_D301N_R334H_Q342E_V396F 0.8   8.7E+05 UGT76G1var74 I295T_I373L_S375R_Y397Q_Q432E 0.6   9.6E+04 UGT76G1var75 F41L_A239I_Q266S_S375M_P382M 0.8 −1.3E+05 UGT76G1var76 F22Y_A239I_L246F_I295M_R334K 2.6   7.2E+05 UGT76G1var77 A239V_F265I_I295T_D301N_K393G 1.9   4.4E+05 UGT76G1var78 V279I_V300A_V310I_I335V_S357C 3.2   8.2E+05 UGT76G1var79 E224D_T284I_V366I_I373L_K393G 8.5   3.8E+06 UGT76G1var80 L243P_L379A_S389E_Q425E_Q432E 1.0   2.1E+05 UGT76G1var81 A33G_T263S_S274G_V279I_Y397E 15.0   6.5E+06 UGT76G1var82 E224D_L243A_F265L_R334H_A352G 1.1   2.5E+05 UGT76G1var83 I43V_Q342E_S357N_S375R_L379G 0.5   4.3E+04 UGT76G1var84 F22L_Q266S_F314S_A352G_S357C 1.2   2.3E+05 UGT76G1var85 T284L_G348P_F377C_P382M_N409R 1.8   4.0E+05 UGT76G1var86 E224A_T284L_V396F_Y397E_I407V 1.6   3.8E+05 UGT76G1var87 S241I_L243A_V300A_F314S_N409R 35.7   2.1E+07 UGT76G1var88 A239V_T284I_V310I_Q342K_L379A 1.6   3.8E+05 UGT76G1var89 F41L_E229A_E231A_F265L_P272A 1.2   2.1E+05 UGT76G1var90 E231A_S241I_S274G_Y397Q_Q425E 34.5   1.9E+07 UGT76G1var91 E224A_L246F_T263S_F2651Q342K 1.2   2.3E+05 UGT76G1var92 K303G_S357N_V366I_V394I_I407V 1.6   3.6E+05 UGT76G1var93 I43V_Q266E_S375M_S389E_V394I 1.8   4.5E+05 UGT76G1var94 Q266E_P272A_R334K_G348P_L379G 72.0   7.9E+07 UGT76G1var95 A33G_I295M_K303G_I335V_A385T −1.3 −1.7E+05 UGT76G1var96 F22L_E229A_L243P_F377C_A385T 1.2   2.7E+05 *Mutations are noted as follows: original amino acid-position-new amino acid: For example the mutation of an alanine at position 33 to a glycine is noted as A33G.

Example 27 In-Vivo Production of UGTSL2

UGTSL2 (GI_460410132/XP_004250485.1) amino acid sequence: (SEQ ID NO: 9) MATNLRVLMFPWLAYGHISPFLNIAKQLADRGFLIYLCSTRINLESIIKK IPEKYADSIHLIELQLPELPELPPHYHTTNGLPPHLNPTLHKALKMSKPN FSRILQNLKPDLLIYDVLQPWAEHVANEQNIPAGKLLTSCAAVFSYFFSF RKNPGVEFPFPAIHLPEVEKVKIREILAKEPEEGGRLDEGNKQMMLMCTS RTIEAKYIDYCTELCNWKVVPVGPPFQDLITNDADNKELIDWLGTKHENS TVFVSFGSEYFLSKEDMEEVAFALELSNVNFIWVARFPKGEERNLEDALP KGFLERIGERGRVLDKFAPQPRILNHPSTGGFISHCGWNSAMESIDFGVP IIAMPIHNDQPINAKLMVELGVAVEIVRDDDGKIHRGEIAETLKSVVTGE TGEILRAKVREISKNLKSIRDEEMDAVAEELIQLCRNSNKSK.

The pET30A+ vector containing the UGTSL2 gene was introduced in E. coli B121(DE3) by heat shock. The obtained cells were grown in petri-dishes in the presence of Kanamycin and suitable colonies were selected and allowed to grow in liquid LB medium (erlenmeyer flasks). Glycerol was added to the suspension as cryoprotecteur and 400 μL aliquots were stored at −20° C. and at −80° C.

The storage aliquots of E. coli BL21(DE3) containing the pET30A+_UGTSL2 plasmids were thawed and added to 30 mL of LBGKP medium (20 g/L Luria Broth Lennox; 50 mM PIPES buffer pH 7.00; 50 mM Phosphate buffer pH 7.00; 2.5 g/L glucose and 50 mg/L of Kanamycin). This culture was allowed to shake at 135 rpm at 30° C. for 8 h.

The production medium contained 60 g/L of overnight express instant TB medium (Novagen), 10 g/L of glycerol and 50 mg/L of Kanamycin. The preculture was added to 200 mL of this medium and the solution was allowed to stir at 20° C. while taking samples to measure the OD and pH. The culture gave significant growth and a good OD was obtained. After 40 h, the cells were harvested by centrifugation and frozen to obtain 6.22 g of cell wet weight.

Lysis was performed on 1.4 g of cells by addition of Bugbuster Master mix (Novagen) and the lysate was recovered by centrifugation and used fresh.

Example 28 Determination of Activity for Stevioside to Rebaudioside E Conversion with UGTSL and UGTSL2

UGTSL was prepared according to EXAMPLE 22, and UGTSL2 was prepared according to EXAMPLE 27.

Activity tests were performed at 3 mL scale with 600 μL of lysate for the transformation of Stevioside using 0.5 mM of substrate, 2.5 mM of UDP-Glucose and 3 mM MgCl2 in 50 mM Sodium Phosphate buffer at pH 7.2. Samples were taken and analyzed by HPLC. HPLC Analysis. The HPLC assay was performed as described in EXAMPLE 20.

The results for the different enzymes and the corresponding chromatograms are provided below.

Enzyme Stevioside internal conv.1 Rebaudioside reference GI Number Version (reaction time) E formation1 UGTSL 460409128 XP_004249992.1 74% (22 h.) 46% UGTSL2 460410132 XP_004250485.1 77% (2 h.) 50% Note: 1Based on initial concentration of Stevioside

Example 29 Determination of Activity for Rubusoside to Rebaudioside E Conversion with UGTSL and UGTSL2

UGTSL was prepared according to EXAMPLE 22, and UGTSL2 was prepared according to EXAMPLE 27.

Activity tests were performed at 3 mL scale with 600 μL of lysate for the transformation of Rubusoside using 0.5 mM of substrate, 2.5 mM of UDP-Glucose and 3 mM MgCl2 in 50 mM Sodium Phosphate buffer at pH 7.2. Samples were taken and analyzed by HPLC. The HPLC assay was performed as described in EXAMPLE 20.

The results for the different enzymes and the corresponding chromatograms are provided below.

Enzyme Rubusoside Rebaudioside internal GI conv.1 E reference Number Version (reaction time) formation1 UGTSL 460409128 XP_004249992.1 70% (45 h.) 27% UGTSL2 460410132 XP_004250485.1 80% (2 h.) 55% Note: 1Based on initial concentration of Rubusoside

Example 30 Determination of Activity for Rebaudioside A to Rebaudioside D Conversion with UGTSL2

UGTSL2 was prepared according to EXAMPLE 27.

Activity tests were performed at 3 mL scale with 60 μL of lysate for the transformation of Rebaudioside A using 0.5 mM of substrate, 2.5 mM of UDP-Glucose and 3 mM MgCl2 in 50 mM Sodium Phosphate buffer at pH 7.2. Samples were taken and analyzed by HPLC. The HPLC assay was performed as described in EXAMPLE 20.

The result after 23 h. of reaction are provided below.

Enzyme Rebaudioside A Rebaudioside internal GI conv.1 (reaction D reference Number Version time) formation1 UGTSL2 460410132 XP_004250485.1 78% (23 h.) 75% Note: 1Based on initial concentration of Rebaudioside A

Example 31 Identification of Glycosides

The reaction mixtures prepared according to EXAMPLE 30 and incubated for 45 hrs was analyzed by LC-MS, along with Stevia rebaudiana Bertoni leaf extract “MLD1” produced by PureCircle Sdn Bhd (Malaysia), to determine the occurrence of unknown formed glycosides (˜4.5 min, ˜6.7 min, ˜7.0 min, ˜7.3 min and ˜7.7 min) in nature.

An Agilent 1200 series HPLC system, equipped with binary pump (G1312B), autosampler (G1367D), thermostatted column compartment (G1316B), DAD detector (G1315C), connected with Agilent 6110A MSD, and interfaced with “LC/MSD Chemstation” software, was used.

Instrument Conditions

Column Phenomenex Prodigy 3u C18 100A, 4.6 mm × 250 mm, 3 μm Column Temperature 55° C. Detection DAD at 210 nm bw 360 nm MSD (Scan and SIM mode) Mode: ES-API, Negative Polarity Drying gas flow: 13.0 L/min Nebulizer pressure: 30 psig Drying gas temperature: 270° C. Analysis duration  75 min Injected volume  10 μL Flow rate 0.5 mL/min

Mobile Phase Gradient Program

Time (min) A (%): Formic acid 0.1% B (%): Acetonitrile 0 75 25 30 75 25 33 68 32 75 68 32

The assay shows that the compound observed on LC-MS system at 11.77 min is the same as the compound at 3.5 min, in EXAMPLE 23 (C56H90O33; later confirmed as reb M2), and the compound observed at 26.64 min is the same as the compound at 7.6 min, in EXAMPLE 23 (C50H80O28; reb UNK; later confirmed as reb D2). Other isomers of reb M were observed at 13.96 min and also another isomer form of reb D was observed at 25.06 min. All observed compounds occurred in the extract of Stevia rebaudiana Bertoni plant.

Example 32 In Vivo Preparation and Activity Determination of UGTLB

UGTLB (GI_209954733/BAG80557.1) amino acid sequence (SEQ ID NO: 10) MGTEVTVHKNTLRVLMFPWLAYGHISPFLNVAKKLVDRGFLIY LCSTAINLKSTIKKIPEKYSDSIQLIELHLPELPELPPHYHTTNGLPPHL NHTLQKALKMSKPNFSKILQNLKPDLVIYDLLQQWAEGVANEQNIPAVKL LTSGAAVLSYFFNLVKKPGVEFPFPAIYLRKNELEKMSELLAQSAKDKEP DGVDPFADGNMQVMLMSTSRIIEAKYIDYFSGLSNWKVVPVGPPVQDPIA DDADEMELIDWLGKKDENSTVFVSFGSEYFLSKEDREEIAFGLELSNVNF IWVARFPKGEEQNLEDALPKGFLERIGDRGRVLDKFAPQPRILNHPSTGG FISHCGWNSVMESVDFGVPIIAMPIHLDQPMNARLIVELGVAVEIVRDDY GKIHREEIAEILKDVIAGKSGENLKAKMRDISKNLKSIRDEEMDTAAEEL IQLCKNSPKLK.

The pET30A+ vector containing the UGTLB gene was introduced in E. coli B121(DE3) by heat shock. The obtained cells were grown in petri-dishes in the presence of Kanamycin and suitable colonies were selected and allowed to grow in liquid LB medium (erlenmeyer flasks). Glycerol was added to the suspension as cryoprotecteur and 400 μL aliquots were stored at −20° C. and at −80° C.

The storage aliquots of E. coli BL21(DE3) containing the pET30A+_UGTLB plasmids were thawed and added to 30 mL of LBGKP medium (20 g/L Luria Broth Lennox; 50 mM PIPES buffer pH 7.00; 50 mM Phosphate buffer pH 7.00; 2.5 g/L glucose and 50 mg/L of Kanamycine). This culture was allowed to shake at 135 rpm at 30° C. for 8 h.

The production medium contained 60 g/L of overnight express instant TB medium (Novagen), 10 g/L of glycerol and 50 mg/L of Kanamycine. The preculture was added to 200 mL of this medium and the solution was allowed to stir at 20° C. while taking samples to measure the OD and pH. The culture gave significant growth and a good OD was obtained. After 40 h, the cells were harvested by centrifugation and frozen to obtain 5.7 g of cell wet weight.

Lysis was performed on 1.2 g of cells by addition of 6 mL Bugbuster Master mix (Novagen) and the lysate was recovered by centrifugation and used fresh.

Determination of Activity for Stevioside to Rebaudioside E Conversion with UGTLB

Activity tests were performed at 3 mL scale with 600 μL of lysate for the transformation of Stevioside using 0.5 mM of substrate, 2.5 mM of UDP-Glucose and 3 mM MgCl2 in 50 mM Sodium Phosphate buffer at pH 7.2. Samples were taken and analyzed by HPLC according to the method of EXAMPLE 20. The results are provided below.

Stevioside conv.1 Rebaudioside E Enzyme (reaction time) formation1 internal (Retention Time (Retention Time reference GI Number Version ~9.2 min) ~5.4 min) UGTLB 209954733 BAG80557.1 89% (22 h.) 3% Note: 1Based on initial concentration of Stevioside

Determination of Activity for Rubusoside to Rebaudioside E Conversion with UGTLB

Activity tests were performed at 3 mL scale with 600 μL of lysate for the transformation of Rubusoside using 0.5 mM of substrate, 2.5 mM of UDP-Glucose and 3 mM MgCl2 in 50 mM Sodium Phosphate buffer at pH 7.2. Samples were taken and analyzed by HPLC according to the method of EXAMPLE 20. The results are provided below.

Rubusoside conv.1 Rebaudioside E Enzyme (reaction time) formation1 internal (Retention Time (Retention Time reference GI Number Version ~11.2 min) ~5.4 min) UGTLB 209954733 BAG80557.1 65% (5 h.) 4% Note: 1Based on initial concentration of Rubusoside

Determination of Activity for Rebaudioside A to Rebaudioside D Conversion with UGTLB

Activity tests were performed at 3 mL scale with 600 μL of lysate for the transformation of Rebaudioside A using 0.5 mM of substrate, 2.5 mM of UDP-Glucose and 3 mM MgCl2 in 50 mM Sodium Phosphate buffer at pH 7.2. Samples were taken and analyzed by HPLC according to the method of EXAMPLE 20. The results after 23 h. of reaction are provided below.

Enzyme Rebaudioside A Rebaudioside internal conv.1 (reaction D reference GI Number Version time) formation1 UGTLB 209954733 BAG80557.1 72% (22 h.) 10% Note: 1Based on initial concentration of Rebaudioside A

Example 33 Determination of Reaction Products for Rubusoside and Stevioside Conversion with UGTSL, UGTSL2, and UGTLB

Conversion of stevioside with UGTSL and UGTSL2 was conducted in similar manner to Example 28, and the conversion of rubusoside with UGTSL and UGTSL2 was conducted similarly to Example 29. Conversions of rubusoside and stevioside with UGTLB was conducted similarly to Example 32.

The reaction mixtures were analyzed by LCMS to determine all reaction products.

Rubusoside Conversion Products

LC-MS, peak area ratio (%) Sample ID UGT (reaction time) Rub Stev Reb E Reb D S151N15 UGTSL2 (2 hrs) 3.54 2.12 52.88 6.73 S151N17 UGTLB (5 hrs) 13.49 ND 9.21 1.29 S151N22 UGTSL (45 hrs) 7.82 2.37 35.88 3.45

Stevioside Conversion Products

LC-MS, peak area ratio (%) Sample ID UGT (reaction time) Stev Reb E Reb D S151N26 UGTSL2 (2 hrs) 20.01 42.56 1.70 S151N28 UGTLB (2 hrs) 43.11 3.12 ND S151N33 UGTSL (22 hrs) 25.24 49.68 0.54

It can be seen that amongst Rubusoside conversion products, besides stevioside, reb E and reb D, there are at least 3 additional compounds with Molecular Weight of 804. The retention time of these compounds do not match with reb B (also known to have same Molecular Weight as stevioside).

Among stevioside conversion products, besides reb E and reb D, there are at least 3 additional compounds with Molecular Weight of 966. The retention time of these compounds do not match with reb A (also known to have same Molecular Weight as reb E).

Example 34 In Vivo Production of UGT76G1 in S. cerevisiae

UGT76G1 [Stevia rebaudiana] (gi_37993653/gb_AAR06912.1) (SEQ ID NO: 11) MENKTETTVRRRRRIILFPVPFQGHINPILQLANVLYSKGFSITIFHTNF NKPKTSNYPHFTFRFILDNDPQDERISNLPTHGPLAGMRIPIINEHGADE LRRELELLMLASEEDEEVSCLITDALWYFAQSVADSLNLRRLVLMTSSLF NFHAHVSLPQFDELGYLDPDDKTRLEEQASGFPMLKVKDIKSAYSNWQIL KEILGKMIKQTKASSGVIWNSFKELEESELETVIREIPAPSFLIPLPKHL TASSSSLLDHDRTVFQWLDQQPPSSVLYVSFGSTSEVDEKDFLEIARGLV DSKQSFLWVVRPGFVKGSTWVEPLPDGFLGERGRIVKWVPQQEVLAHGAI GAFWTHSGWNSTLESVCEGVPMIFSDFGLDQPLNARYMSDVLKVGVYLEN GWERGEIANAIRRVMVDEEGEYIRQNARVLKQKADVSLMKGGSSYESLES LVSYISSL.

The above mentioned amino acid sequence was codon optimized for expression in S. cerevisiae. Furthermore the yeast consensus sequence AACACA was added before the ATG start codon. The synthetic gene was subcloned in the pYES2 vector using Hind III and Xba I restriction sites. The pYES2_UGT76G1_Sc vector was used to transform chemically competent S. cerevisiae INVSc1 cells (Invitrogen).

The cells were grown on a solid synthetic minimal medium containing 2% glucose lacking Uracil and a single colony was picked and allowed to grow in liquid synthetic minimal medium lacking Uracil (SC-U containing 2% glucose). After centrifugation, the cells were suspended with SC-U (containing 2% glucose) and 60% glycerol/water. Aliquots were stored at −80° C. and one aliquot was used to start a culture in SC-U (containing 2% glucose) for 43 h at 30° C. Part of this culture was centrifuged and suspended in induction medium (SC-U containing 2% galactose) for 19 h 30 at 30° C.

Cells were obtained by centrifugation and lysis with five volumes of CelLytic™ Y Cell Lysis Reagent (Sigma). The lysates were used directly for activity testing (UGT76G1_Sc).

Example 35 Determination of Activity of UGT76G1_Sc for the Conversion of Rebaudioside D to Rebaudioside M

UGT76G1_Sc was prepared according to EXAMPLE 34. Activity tests were performed at 2 mL scale with 200 μL of lysate for the transformation of Rebaudioside D using 0.5 mM of substrate, 2.5 mM of UDP-Glucose and 3 mM MgCl2 in 50 mM Sodium Phosphate buffer at pH 7.2. Samples were taken and analyzed by HPLC according to the method of EXAMPLE 20. The results are shown below.

Rebaudioside Rebaudioside M Enzyme internal D conv.1 selectivity1 reference (reaction time) (Retention Time ~6.7 min) UGT76G 1 _Sc 85% (21h.) 100% Note: 1Based on initial concentration of Rebaudioside D

Example 36 In Vivo Production of UGTSL in S. cerevisiae

UGTSL [Solanum lycopersicum] (gi_460409128/XP_004249992.1 (SEQ ID NO: 12) MSPKLHKELFFHSLYKKTRSNHTMATLKVLMFPFLAYGHISPYLNVAKKL ADRGFLIYFCSTPINLKSTIEKIPEKYADSIHLIELHLPELPQLPPHYHT TNGLPPNLNQVLQKALKMSKPNFSKILQNLKPDLVIYDILQRWAKHVANE QNIPAVKLLTSGAAVFSYFFNVLKKPGVEFPFPGIYLRKIEQVRLSEMMS KSDKEKELEDDDDDDDLLVDGNMQIMLMSTSRTIEAKYIDFCTALTNWKV VPVGPPVQDLITNDVDDMELIDWLGTKDENSTVFVSFGSEYFLSKEDMEE VAFALELSNVNFIWVARFPKGEERNLEDALPKGFLERIGERGRVLDKFAP QPRILNHPSTGGFISHCGWNSAMESIDFGVPIIAMPMHLDQPMNARLIVE LGVAVEIVRDDDGKIHRGEIAETLKGVITGKTGEKLRAKVRDISKNLKTI RDEEMDAAAEELIQLCRNGN.

The above mentioned amino acid sequence was codon optimized for expression in S. cerevisiae. Furthermore the yeast consensus sequence AACACA was added before the ATG start codon. The synthetic gene was subcloned in the pYES2 vector using Hind III and Xba I restriction sites. The pYES2_UGTSL_Sc vector was used to transform chemically competent S. cerevisiae INVSc1 cells (Invitrogen).

The cells were grown on a solid synthetic minimal medium containing 2% glucose, lacking Uracil and a single colony was picked and allowed to grow in liquid synthetic minimal medium lacking Uracil (SC-U containing 2% glucose). After centrifugation, the cells were suspended with SC-U (containing 2% glucose) and 60% glycerol/water. Aliquots were stored at −80° C. and one aliquot was used to start a culture in SC-U (containing 2% glucose) for 43 h at 30° C. Part of this culture was centrifuged and suspended in induction medium (SC-U containing 2% galactose) for 19 h 30 at 30° C.

Cells were obtained by centrifugation and lysis with five volumes of CelLytic™ Y Cell Lysis Reagent (Sigma). The lysates were used directly for activity testing (UGTSL_Sc).

Example 37 Determination of Activity of UGTSL_Sc for the Conversion of Rebaudioside A to Rebaudioside D

UGTSL_Sc was prepared according to EXAMPLE 36. Activity tests were performed at 2 mL scale with 200 μL of lysate for the transformation of Rebaudioside A using 0.5 mM of substrate, 2.5 mM of UDP-Glucose and 3 mM MgCl2 in 50 mM Sodium Phosphate buffer at pH 7.2. Samples were taken and analyzed by HPLC according to the method of EXAMPLE 20. The results are provided below.

Enzyme internal Rebaudioside A conv.1 (reaction Rebaudioside D reference time) selectivity1 UGTSL_Sc 46% (4h) 42% Note: 1Based on initial concentration of Rebaudioside A

Example 38 Isolation of Rebaudioside M

The amount of the product mixture of Example 14 was not large enough to separate via preparative HPLC methods. Accordingly, analytical HPLC with a series of injections was used to separate the components of the mixture. Separation was conducted according to the method described above in Example 14 to provide two fractions corresponding to the two main peaks in the HPLC trace of FIG. 3: Fraction A (retention time 24.165 minutes) and Fraction B (retention time 31.325 minutes).

The retention time of Fraction A was consistent with reb D, indicating unreacted starting material from the biotransformation reaction.

The retention time of purified Fraction B was consistent with reb M, indicating successful biotransformation from reb D. The identity of the material collected in Fraction B as reb M was confirmed by co-injection of purified Fraction B with a reb M standard (available from PureCircle). Both Fraction B and the reb M standard were found to elute at the same retention time (FIG. 7), indicating Fraction B was reb M.

The identity of Fraction B as reb M was also separately confirmed by NMR and HRMS. For sampling, Fraction B was concentrated under rotary evaporator, freeze dried and dried for 40 h at 40° C.

The NMR sample was dissolved in deuterated pyridine (C5D5N) and spectra were acquired on a Varian Unity Plus 600 MHz instrument using standard pulse sequences. The NMR spectra of Fraction B was compared to the NMR spectra of reb M. An overlay of the two spectra showed consistency of peaks of Fraction B with reb M. A table of the NMR assignments for reb M is shown below:

1H and 13C NMR Spectral Data for Rebaudioside M in C5D5Na-c

Position 13C NMR 1H NMR  1 40.3 0.75 t (13.2)   1.76 m  2 19.6 1.35 m   2.24 m  3 38.4 1.01 m   2.30 d (13.3)  4 44.3 —  5 57.4 1.06 d (12.8)  6 23.5 2.23 m 2.41 q (13.2)  7 42.6 1.41 m   1.80 m  8 41.2 —  9 54.3 0.91 d (7.7) 10 39.7 — 11 20.2 1.65 m 1.75 m 12 38.5 1.86 m 2.73 m 13 87.6 — 14 43.3 2.02 m 2.74 m 15 46.5 1.88 d (16.4) 2.03 m 16 153.3 — 17 104.9 4.90 s 5.69 s 18 28.2 1.32 s 19 176.9 — 20 16.8 1.38 s  1′ 94.9 6.39 d (8.2)  2′ 76.9 4.51 t (8.5)  3′ 88.6 5.09 t (8.5)  4′ 70.1 4.18 m  5′ 78.4 4.13 m  6′ 61.8 4.20 m   4.31 m  1″ 96.2 5.46 d (7.1)  2″ 81.4 4.13 m  3″ 87.9 4.98 t (8.5)  4″ 70.4 4.07 t (9.6)  5″ 77.7 3.94 m  6″ 62.6 4.19 m   4.32 m  1′″ 104.8 5.48 d (7.7)  2′″ 75.8 4.15 m  3′″ 78.6 4.13 m  4′″ 73.2 3.98 m  5′″ 77.6 3.74 ddd (2.8, 6.4, 9.9)  6′″ 64.0 4.27 m   4.51 m  1″″ 103.9 5.45 d (7.5)  2″″ 75.6 3.98 m  3″″ 77.8 4.50 t (7.8)  4″″ 71.3 4.14 m  5″″ 78.0 3.99 m  6″″ 62.1 4.20 m   4.32 m  1′″″ 104.2 5.81 d (7.2)  2′″″ 75.5 4.20 m  3′″″ 78.4 4.20 m  4′″″ 73.6 4.10 m  5′″″ 77.8 3.90 ddd (2.8, 6.4, 9.9)  6′″″ 64.0 4.32 m   4.64 d (10.3)  1″″″ 104.1 5.31 d (8.0)  2″″″ 75.5 3.95 m  3″″″ 78.0 4.37 t (9.1)  4″″″ 71.1 4.10 m  5″″″ 78.1 3.85 ddd (1.7, 6.1, 9.9)  6″″″ 62.1 4.10 m 4.32 m a assignments made on the basis of COSY, HMQC and HMBC correlations; b Chemical shift values are in δ (ppm); c Coupling constants are in Hz.

HRMS was generated with a Waters Premier Quadropole Time-of-Flight (Q-TOF) mass spectrometer equipped with an electrospray ionization source operated in the positive-ion mode. The sample was dissolved in methanol and eluted in 2:2:1 methanol:acetonitrile:water and introduced via infusion using the onboard syringe pump. The presence of reb M was confirmed by a [M+Na]+ adduct at m/z 1313.5265, which corresponds to a molecular formula of C56H90O33

Example 39 Isolation and Characterization of Reb D2 Crude Reaction Sample.

The sample, Lot CB-2977-106, used for isolation, was prepared according to Example 22 with UGTSL (GI #460409128).

HPLC Analysis.

Preliminary HPLC analyses of samples were performed using a Waters 2695 Alliance System with the following method: Phenomenex Synergi Hydro-RP, 4.6×250 mm, 4 μm (p/n 00G-4375-E0); Column Temp: 55° C.; Mobile Phase A: 0.0284% ammonium acetate (NH4OAc) and 0.0116% acetic acid (HOAc) in water; Mobile Phase B: Acetonitrile (MeCN); Flow Rate: 1.0 mL/min; Injection volume: 10 μL. Detection was by UV (210 nm) and CAD.

Gradient:

Time (min) % A % B 0.0-8.5 75 25 10.0 71 29 16.5 70 30 18.5-24.5 66 34 26.5-29.0 48 52 31-37 30 70 38 75 25

Analyses of semi-preparative purification fractions were performed with the following method: Waters Atlantis dC18, 4.6×100 mm, 5 μm (p/n 186001340); Mobile Phase A: 25% MeCN in water; Mobile Phase B: 30% MeCN in water; Flow Rate: 1.0 mL/min; Injection volume: 10 μL. Detection was by CAD.

Gradient:

Time (min) % A % B 0.0-5.0 100 0 20 20 80 25 20 80 30 100 0

LC-MS.

Preliminary analysis of the semi-synthetic steviol glycoside mixture was carried out on a Waters AutoPurification HPLC/MS System with a Waters 3100 Mass Detector operating in negative ion mode. Analysis of the sample was performed using the following method: Phenomenex Synergi Hydro-RP, 4.6×250 mm, 4 μm (p/n 00G-4375-E0); Column Temp: 55° C.; Mobile Phase A: 0.0284% NH4OAc and 0.0116% HOAc in water; Mobile Phase B: Acetonitrile; Flow Rate: 1.0 mL/min; Injection volume: 10 pt. Detection was by UV (210 nm), and MSD (−ESI m/z 500-2000). Gradient conditions were as listed above.

Isolation by HPLC.

The purification was performed in two steps. The first method used for the semi-preparative purification is summarized below. Column: Waters Atlantis dC18, 30×100 mm, 5 μm (p/n 186001375); Mobile Phase A: 25% MeCN in water; Mobile Phase B: 30% MeCN in water; Flow Rate: 45 mL/min; Injection load: 160 mg dissolved in 20 mL of water. Detection was by UV (205 nm).

Gradient:

Time (min) % A % B 0.0-5.0 100 0 20 20 80 25 20 80 30 100 0

The secondary purification used the same column and conditions, but isocratic mobile phase: 20% MeCN in water.

Purification from Natural Extracts.

The purification was performed in three steps. The first method used for the preparative purification is summarized below. Primary Process: Waters Symmetry C18, 50×250 mm, 7 μm (p/n WAT248000); Isocratic mobile phase: 50% methanol (MeOH) in water with 0.05% HOAc; Flow Rate: 85 mL/min; Injection load: 6 g crude extract dissolved in 50 mL of mobile phase. Detection was by UV (210 nm). Following the elution of target analytes, the column was flushed with 85% MeOH in water.

Secondary Process: Waters Symmetry Shield RP18, 50×250 mm, 7 μm (p/n WAT248000); Isocratic mobile phase: 20% MeCN in water; Flow Rate: 100 mL/min; Injection load: 0.5 g primary fraction dissolved in 30 mL of water. Detection was by UV (210 nm).

Tertiary Process: Waters Symmetry Shield RP18, 50×250 mm, 7 μm (p/n WAT248000); Isocratic mobile phase: 20% MeCN in water; Flow Rate: 100 mL/min; Injection load: 0.5 g secondary fraction dissolved in 30 mL of water. Detection was by UV (210 nm).

MS and MS/MS.

MS and MS/MS data were generated with a Waters QT of Premier mass spectrometer equipped with an electrospray ionization source. Samples were analyzed by negative ESI. Samples were diluted with H2O:acetonitrile (1:1) by 50 fold and introduced via infusion using the onboard syringe pump. The samples were diluted to yield good s/n which occurred at an approximate concentration of 0.01 mg/mL.

NMR.

The sample was prepared by dissolving 1-2 mg in 150 μL of pyridine-d5 and NMR data were acquired on a Bruker Avance 500 MHz instrument with a 2.5 mm inverse detection probe. The 1H NMR spectrum was referenced to the residual solvent signal (δH 8.74 and δC 150.35 for pyridine-d5).

Results and Discussion Isolation and Purification.

Isolation was performed on steviol glycoside mixture, Lot number CB-2977-106, prepared according to Example 22 with UGTSL (GI #460409128) The material was analyzed by LC-MS using the method described above and results are provided in FIG. 6. The targeted peak of interest was that at 7.7 min in the TIC chromatogram. The mass spectrum of this peak provided a [M-H]− ion at m/z 1127.6. The provided sample was preliminarily processed in a single injection (160 mg) using the first method condition provided above. This method fractionated the material into ‘polar’ and ‘non-polar’ mixtures of glycosides. The ‘polar’ mixture was then reprocessed using the second-step conditions above. From this semi-preparative collection, the compound was isolated with a purity >99% (CAD, AUC). Following the purification, the combined fractions were concentrated by rotary evaporation at 35° C. and lyophilized. Approximately 1-2 mg was obtained for characterization.

Mass Spectrometry.

The ESI-TOF mass spectrum acquired by infusing a sample showed a [M-H]− ion at m/z 1127.4709. The mass of the [M-H]− ion was in good agreement with the molecular formula C50H80O28 (calcd for C50H79O28: 1127.4758, error: −4.3 ppm). The MS data confirmed a nominal mass of 1128 Daltons with the molecular formula, C50H80O28.

The MS/MS spectrum (selecting the [M-H]− ion at m/z 1127.5 for fragmentation) indicated the loss of two glucose units and sequential loss of three glucose moieties at m/z 641.3187, 479.2655 and 317.2065.

NMR Spectroscopy.

A series of NMR experiments including 1H NMR (FIG. 8), 13C NMR (FIGS. 9 and 10), 1H-1H COSY (FIG. 11), HSQC-DEPT (FIG. 12), HMBC (FIGS. 13 and 14), NOESY (FIG. 15) and 1D-TOCSY were performed to allow assignment of the compound. In the 1H NMR acquired after ˜46 hrs of sample preparation, the anomeric resonance at δH 5.04 is resolved which was obscured by the solvent (HOD) in the original spectrum (FIG. 8)

The 1H, 1H-1H COSY, 1H-13C HSQC-DEPT and 1H-13C HMBC NMR data indicated that the central core of the glycoside is a diterpene. The presence of five anomeric protons observed in the 1H and 1H-13C HSQC-DEPT spectra confirm five sugar units in the structure. The methylene 13C resonance at δC 69.9 in the 1H-13C HSQC-DEPT spectrum indicated the presence of a 1→6 sugar linkage in the structure. The linkages of sugar units were assigned using 1H-13C HMBC and 1D-TOCSY correlations.

A HMBC correlation from the methyl protons at δH 1.29 to the carbonyl at δC 177.7 allowed assignment of one of the tertiary methyl groups (C-18) as well as C-19 and provided a starting point for the assignment of the rest of the aglycone. Additional HMBC correlations from the methyl protons (H-18) to carbons at δC 38.9, 45.0, and 57.8 allowed assignment of C-3, C-4, and C-5. Analysis of the 1H-13C HSQC-DEPT data indicated that the carbon at δC 38.9 was a methylene group and the carbon at δC 57.8 was a methine which were assigned as C-3 and C-5, respectively. This left the carbon at δC 45.0, which did not show a correlation in the HSQC-DEPT spectrum, to be assigned as the quaternary carbon, C-4. The 1H chemical shifts for C-3 (δH 0.98 and 2j.36) and C-5 (δH 1.04) were assigned using the HSQC-DEPT data. A COSY correlation between one of the H-3 protons (δH 0.98) and a proton at δH 1.43 allowed assignment of one of the H-2 protons which in turn showed a correlation with a proton at δH 0.75 which was assigned to C-1. The remaining 1H and 13C chemical shifts for C-1 and C-2 were then assigned on the basis of additional COSY and HSQC-DEPT correlations and are summarized in the table below.

1H and 13C NMR (500 and 125 MHz, Pyridine-d5), Assignments of Reb D2.

Reb D2 Position 13C 1H 1 41.3 0.75 t (11.0) 1.76 m 2 19.9 1.43 m 2.20 m 3 38.9 0.98 m 2.36 d (12.1) 4 45.0 — 5 57.8 1.04 d (12.5) 6 22.7 1.92 m 2.43 m 7 42.2 1.22 m 1.30 m 8 43.1 — 9 54.5 0.88 brs 10 40.3 — 11 21.1 1.65 m 1.69 m 12 37.5 1.99 m 2.25 m 13 87.1 — 14 44.5 1.80 d (11.7) 2.65 d (11.7) 15 48.3 1.31 m 2.04 brs 16 154.7 — 17 105.2 5.01 s 5.64 s 18 28.8 1.29 s 19 177.7 — 20 16.0 1.30 s

The other tertiary methyl singlet, observed at δH 1.30 showed HMBC correlations to C-1 and C-5 and was assigned as C-20. The methyl protons showed additional HMBC correlations to a quaternary carbon (δC 40.3) and a methine carbon (δC 54.5) which were assigned as C-10 and C-9, respectively. COSY correlations between H-5 (δH 1.04) and protons at δH 1.92 and 2.43 then allowed assignment of the H-6 protons which in turn showed correlations to protons at δH 1.22 and 1.30 which were assigned to C-7. The 13C chemical shifts for C-6 (δC 22.7) and C-7 (δC 42.2) were then determined from the HSQC-DEPT data. COSY correlations between H-9 (δH 0.88) and protons at δH 1.65 and 1.69 allowed assignment of the H-11 protons which in turn showed COSY correlations to protons at δH 1.99 and 2.25 which were assigned as the H-12 protons. The HSQC-DEPT data was then used to assign C-11 (δC 21.1) and C-12 (δC 37.5). HMBC correlations from the H-12 proton (δH 2.25) to carbons at δC 87.1 and 154.7 allowed assignment of C-13 and C-16, respectively. The olefinic protons observed at δH 5.01 and 5.64 showed HMBC correlations to C-13 and were assigned to C-17 (δC 105.2 via HSQC-DEPT). The olefinic protons H-17 and the methine proton H-9 showed HMBC correlations to a carbon at δC 48.3 which was assigned as C-15. An additional HMBC correlation from H-9 to a methylene carbon at δC 44.5 then allowed assignment of C-14. The 1H chemical shifts at C-14 (δH 1.80 and 2.65) and C-15 (δH 1.31 and 2.04) were assigned using the HSQC-DEPT data.

Correlations observed in the NOESY spectrum were used to assign the relative stereochemistry of the central diterpene core. In the NOESY spectrum, NOE correlations were observed between H-14 and H-20 indicating that H-14 and H-20 are on the same face of the rings. Similarly, NOE correlations were observed between H-9 and H-5; H-9 and H-18 as well as H-5 and H-18 but NOE correlations were not observed between H-9 and H-14 indicating that H-5, H-9 and H-18 were on the opposite face of the rings compared to H-14 and H-20. These data indicated that the relative stereochemistry in the central core was retained during the glycosylation step.

The key HMBC and COSY correlations used to assign the aglycone region are provided below:

Analysis of the 1H-13C HSQC-DEPT data confirmed the presence of five anomeric protons. Three of the anomeric protons were well resolved at δH 6.02 (δC 96.1), 5.57 (δC 105.3), and 5.34 (δC 105.3) in the 1H NMR spectrum. The remaining two anomeric protons observed at δH 5.04 (δC 105.6) and 5.07 (δC 98.7) which were obscured by solvent (HOD) resonance in the 1H spectrum were identified by 1H-13C HSQC-DEPT data. The anomeric proton observed at δH 6.02 showed HMBC correlation to C-19 which indicated that it corresponds to the anomeric proton of GlcI. Similarly, the anomeric proton observed at δH 5.07 showed an HMBC correlation to C-13 allowing it to be assigned as the anomeric proton of GlcII.

The GlcI anomeric proton (δH 6.02) showed a COSY correlation to a proton at δH 4.07 was assigned as GlcI H-2 which in turn showed a COSY correlation to a proton at δH 4.22 (GlcI H-3) which showed a COSY correlation with a proton at δH 4.12 (GlcI H-4). Due to data overlap, the COSY spectrum did not allow assignment of H-5 or the H-6 protons. Therefore, a series of 1D-TOCSY experiments were performed using selective irradiation of the GlcI anomeric proton with several different mixing times. In addition to confirming the assignments for GlcI H-2 through H-4, the 1D-TOCSY data showed a proton at δH 4.04 assigned as GlcI H-5 and a proton at δH 4.68 assigned as one of the GlcI H-6 protons. The latter proton was also used for 1D-TOCSY experiments. The selective irradiation of H-6 with several different mixing times also confirmed the assignment of GlcI H-1 to H-5 as well as the remaining methylene proton of H-6 (δH 4.30). Assignment of the 13C chemical shifts for GlcI C-2 (δC 74.2), C-3 (δC 79.1), C-4 (δC 72.1), C-5 (δC 78.5), and C-6 (δC 69.9) was determined using the 1H-13C HSQC-DEPT data to complete the assignment of GlcI. Furthermore, the presence of a methylene 13C resonance at δC 69.9 in the 1H-13C HSQC-DEPT spectrum indicated a 1→6 sugar linkage of GlcI in the structure.

Out of four remaining unassigned glucose moieties, one was assigned as a substituent at C-6 of GlcI on the basis of 1H-13C HSQC-DEPT, HMBC, and 1D-TOCSY correlations. The relatively downfield shift of a methylene 13C resonance of GlcI at δC 69.9 in the HSQC-DEPT spectrum indicated a 1→6 sugar linkage of GlcI. The anomeric proton observed at δH 5.04 showed HMBC correlation to GlcI C-6 and was assigned as the anomeric proton of GlcV. Similarly, methylene protons of GlcI showed HMBC correlations to anomeric carbon of GlcV confirming the presence of a 1→6 sugar linkage between GlcI and GlcV. The GlcV anomeric proton showed a COSY correlation to a proton at δH 4.00 which was assigned as GlcV H-2 which in turn showed a COSY correlation to a proton at δH 4.22 (GlcV H-3). Due to data overlap, the COSY spectrum did not allow assignment of GlcV H-4 based on the COSY correlation of GlcV H-3. However, in the HMBC spectrum, GlcV H-3 showed a correlation to GlcV C-5 (δC 78.9). In HSQC-DEPT spectrum, GlcV C-5 showed a correlation to δH 3.89 (GlcV H-5). The GlcV H-5 showed COSY correlations to δH 4.21, 4.37, and 4.48. In the HSQC-DEPT spectrum, δH 4.21 showed a correlation to δC 71.4 (GlcV H-4), while δH 4.37 and 4.48 showed a correlation to δC 63.1 and were assigned to GlcV H-6a and H-6b, respectively. Assignment of the 13C chemical shifts for GlcV C-2 (δC 75.7) and C-3 (δC 79.1) was determined using the 1H-13C HSQC-DEPT data to complete the assignment of GlcV.

A summary of the 1H and 13C chemical shifts for the glycoside at C-19 are shown in the following table:

1H and 13C NMR (500 and 125 MHz, Pyridine-d5), Assignments of the Reb D2 C-19 Glycoside.

Reb D2 Position 13C 1H GlcI-1  96.1 6.02 d (8.1) GlcI-2  74.2 4.07 m GlcI-3  79.1# 4.22 m# GlcI-4  72.1 4.12 m GlcI-5  78.5 4.04 m GlcI-6  69.9 4.30 m 4.68 d (10.7) GlcV-1 105.6 5.04 (8.1) GlcV-2  75.7 4.00 m GlcV-3  79.1# 4.22 m# GlcV-4  71.4 4.21 m GlcV-5  78.9 3.89 m GlcV-6  63.1 4.37 m 4.48 m 1H and 13C values can be exchangeable between positions Glc1-3, GlcV-3and GlcIV-3.

A summary of the key HMBC, COSY, and 1D-TOCSY correlations used to assign the C-19 glycoside region are provided below.

Assignment of GlcII was carried out in a similar manner. The GlcII anomeric proton (δH 5.07) showed a COSY correlation to a proton at δH 4.37, assigned as GlcII H-2, which in turn showed a COSY correlation to a proton at δH 4.18 (GlcII H-3). This latter proton showed an additional correlation with a proton at δH 3.88 (GlcII H-4) which also showed a COSY correlation to a proton at δH 3.79 (GlcII H-5). GlcII H-5 also showed a COSY correlation to GlcII H-6 protons (δH 4.08 and 4.46). Assignment of the 13C chemical shifts for GlcII C-2 (δC 81.3), C-3 (δC 88.4), C-4 (δC 71.1), C-5 (δC 77.9), and C-6 (δC 63.2) was determined using the HSQC-DEPT data. HMBC correlations from GlcII H-3 to C-2 and C-4 and also from GlcII H-4 to C-2 and C-5 confirmed the assignments made above. Additional HMBC correlations of GlcII H-4 to GlcII C-6 further support to complete the assignment of GlcII.

Two of the remaining unassigned glucose moieties were assigned as substituents at C-2 and C-3 of GlcII on the basis of HMBC correlations. The anomeric proton observed at δH 5.57 showed a HMBC correlation to GlcII C-2 and was assigned as the anomeric proton of GlcIII. The anomeric proton observed at δH 5.34 showed a HMBC correlation to GlcII C-3 and was assigned as the anomeric proton of GlcIV. The reciprocal HMBC correlations from GlcII H-2 to the anomeric carbon of GlcIII and from GlcII H-3 to the anomeric carbon of GlcIV were also observed.

The anomeric proton of GlcIII (δH 5.57) showed a COSY correlation with a proton at δH 4.19 which was assigned as GlcIII H-2. Due to data overlap, the COSY spectrum did not allow assignment of H-3 to H-6 protons. Therefore, a series of 1D-TOCSY experiments were performed using selective irradiation of the GlcIII anomeric proton with several different mixing times. In addition to confirming the assignments for GlcIII H-2, the 1D-TOCSY data showed protons at δH 4.24 (GlcIII H-3), δH 4.27 (GlcIII H-4), and δH 3.94 (GlcIII H-5). Once H-4 was assigned using 1D-TOCSY data, COSY correlations from H-4 to H-5 and in turn to H-6 were used to assign H-6. In the COSY spectrum, GlcIII H-4 showed a correlation to GlcIII H-5, which in turn showed COSY correlations to δH 4.41 and 4.50 of GlcIII H-6a and H-6b, respectively. The 13C chemical shifts for GlcIII C-2 (δC 76.8), C-3 (δC 78.9), C-4 (δC 72.4), C-5 (δC 78.8), and C-6 (δC 63.5) were then determined using the 1H-13C HSQC-DEPT correlations to complete the assignment of GlcIII.

The anomeric proton of GlcIV (δH 5.34) showed a COSY correlation with a proton at δH 4.06 which was assigned as GlcIV H-2. Due to data overlap, the COSY spectrum did not allow assignment of H-3 to H-6 protons. Therefore, a series of 1D-TOCSY experiments were performed using selective irradiation of the GlcIV anomeric proton with several different mixing times. In addition to confirming the assignments for GlcIV H-2, the 1D-TOCSY data showed protons at δH 4.22 (GlcIV H-3), δH 4.18 (GlcIV H-4), and δH 4.10 (GlcIV H-5). Once H-4 was assigned using 1D-TOCSY data, COSY correlations from H-4 to H-5 and in turn to H-6 were used to assign H-6. In the COSY spectrum, GlcIV H-4 showed a correlation to GlcIV H-5, which in turn showed COSY correlations to δH 4.32 and 4.58, GlcIV H-6a and H-6b, respectively. The 13C chemical shifts for GlcIV C-2 (δC 75.8), C-3 (δC 78.9), C-4 (δC 72.0), C-5 (δC 79.3), and C-6 (δC 62.9) were then determined using the 1H-13C HSQC-DEPT correlations to complete the assignment of GlcIV.

The large coupling constants observed for the anomeric protons of the glucose moieties at δH 6.02 (d, J=8.1 Hz), 5.57 (d, J=7.6 Hz), 5.34 (d, J=7.9 Hz) and δH 5.04 (d, J=8.1 Hz), suggested their β-orientation. While the remaining anomeric proton at δH 5.07 was obscured by the solvent resonance (HDO) it's coupling constant (J=˜8 Hz) evident from 1D TOCSY data also indicated β-orientation.

A summary of the 1H and 13C chemical shifts for the glycoside at C-13 are shown in the table below:

1H and 13C NMR (500 and 125 MHz, Pyridine-d5), Assignments of the Reb D2 C-13 Glycoside

Reb D2 Position 13C 1H GlcII-1  98.7 5.07 (~8)* GlcII-2  81.3 4.37 m GlcII-3  88.4 4.18 m GlcII-4  71.1 3.88 m GlcII-5  77.9 3.79 m GlcII-6  63.2 4.08 m 4.47 m GlcIII-1 105.3 5.57 d (7.6) GlcIII-2  76.8 4.19 m GlcIII-3  78.9 4.24 m GlcIII-4  72.4 4.27 m GlcIII-5  78.8 3.94 m GlcIII-6  63.5 4.41 m 4.50 m GlcIV-1 105.3 5.34 d (7.9) GlcIV-2  75.8 4.06 m GlcIV-3  78.9# 4.22 m# GlcIV-4  72.0 4.18 m GlcIV-5  79.3 4.10 m GlcIV-6  62.9 4.32 m 4.58 m *Anomeric proton was obscured by solvent (HDO) resonance, coupling constant value obtained from 1D-TOCSY data. #1H and 13C values can be exchangeable between Glc1-3, GlcV-3and GlcIV-3.

A summary of the key HMBC, COSY, and 1D-TOCSY correlations used to assign the C-13 glycoside region are provided below:

The chemical name of the compound is 13-[(2-O-β-D-glucopyranosyl-3-O-β-D-glucopyranosyl-β-D-glucopyranosyl)oxy] ent-kaur-16-en-19-oic acid-[(6-O-β-D-glucopyranosyl-β-D-glucopyranosyl) ester] (rebaudioside D2 or reb D2). The compound is an isomer of rebaudioside D.

Example 40 Isolation and Characterization of Reb M2 Crude Reaction Sample.

The sample, Lot CB-2977-106, used for isolation was prepared according to Example 22 with UGTSL (GI #460409128).

HPLC Analysis.

Preliminary HPLC analyses was performed using a Waters 2695 Alliance System with the following method: Phenomenex Synergi Hydro-RP, 4.6×250 mm, 4 μm (p/n 00G-4375-E0); Column Temp: 55° C.; Mobile Phase A: 0.0284% NH4OAc and 0.0116% HOAc in water; Mobile Phase B: Acetonitrile (MeCN); Flow Rate: 1.0 mL/min; Injection volume: 10 μL. Detection was by UV (210 nm) and CAD.

Gradient:

Time (min) % A % B 0.0-5.0 100 0 20 20 80 25 20 80 30 100 0

Analyses of semi-preparative purification fractions were performed with the following method: Waters Atlantis dC18, 4.6×100 mm, 5 μm (p/n 186001340); Mobile Phase A: 25% MeCN in water; Mobile Phase B: 30% MeCN in water; Flow Rate: 1.0 mL/min; Injection volume: 10 μL. Detection was by CAD.

Gradient:

Time (min) % A % B 0.0-8.5 75 25 10.0 71 29 16.5 70 30 18.5-24.5 66 34 26.5-29.0 48 52 31-37 30 70 38 75 25

LC-MS.

Preliminary analysis of the semi-synthetic steviol glycoside mixture was carried out on a Waters AutoPurification HPLC/MS System with a Waters 3100 Mass Detector operating in negative ion mode. Analysis of the sample was performed using the following method: Phenomenex Synergi Hydro-RP, 4.6×250 mm, 4 μm (p/n 00G-4375-E0); Column Temp: 55° C.; Mobile Phase A: 0.0284% NH4OAc and 0.0116% HOAc in water; Mobile Phase B: MeCN; Flow Rate: 1.0 mL/min; Injection volume: 10 μL. Detection was by UV (210 nm), and MSD (−ESI m/z 500-2000). Gradient conditions were as listed above.

Isolation by HPLC.

The purification was performed in two steps. The first method used for the semi-preparative purification is summarized below. Column: Waters Atlantis dC18, 30×100 mm, 5 μm (p/n 186001375); Mobile Phase A: 25% MeCN in water; Mobile Phase B: 30% MeCN in water; Flow Rate: 45 mL/min; Injection load: 160 mg dissolved in 20 mL of water. Detection was by UV (205 nm).

Gradient:

Time (min) % A % B 0.0-5.0 100 0 20 20 80 25 20 80 30 100 0

The secondary purification used the same column and conditions, but isocratic mobile phase: 20% MeCN in water.

MS and MS/MS.

MS and MS/MS data were generated with a Waters QTof Premier mass spectrometer equipped with an electrospray ionization source. Samples were analyzed by negative ESI. Samples were diluted with H2O:MeCN (1:1) by 50 fold and introduced via infusion using the onboard syringe pump. The samples were diluted to yield good s/n which occurred at an approximate concentration of 0.01 mg/mL.

NMR.

The sample was prepared by dissolving ˜1.0 mg in 150 μL of D2O and NMR data were acquired on a Bruker Avance 500 MHz instrument with a 2.5 mm inverse detection probe. The 1H NMR and 13C NMR spectra were referenced to the residual solvent signal HDO (δH 4.79 ppm) and TSP (δC 0.00 ppm), respectively.

Results and Discussion Isolation and Purification.

Isolation was performed using on a steviol glycoside mixture, Lot number CB-2977-106, prepared according to Example 22 with UGTSL (GI #460409128). The material was analyzed by LC-MS using the method described above (FIG. 6). The targeted peak of interest was that at 4.1 min in the TIC chromatogram. The mass spectrum of this peak provided a [M-H]− ion at m/z 1289.7. The provided sample was preliminarily processed in a single injection (160 mg) using the first method condition provided above. This method fractionated the material into ‘polar’ and ‘non-polar’ mixtures of glycosides. The ‘polar’ mixture was then reprocessed using the second-step conditions provided above. From this semi-preparative collection, the peak was isolated with a purity >99% (CAD, AUC). Following the purification, the fractions were concentrated by rotary evaporation at 35° C. and lyophilized. Approximately 1 mg was obtained.

Mass Spectrometry.

The ESI-TOF mass spectrum acquired by infusing a sample of CC-00300 showed a [M-H]− ion at m/z 1289.5266. The mass of the [M-H]− ion was in good agreement with the molecular formula C56H90O33 (calcd for C56H89O33: 1289.5286, error: −1.6 ppm) expected for reb M2. The MS data confirmed that CC-00300 has a nominal mass of 1290 Daltons with the molecular formula, C56H90O33.

The MS/MS spectrum (selecting the [M-H]− ion at m/z 1289.5 for fragmentation) indicated the loss of three glucose units at m/z 803.3688 and sequential loss of three glucose moieties at m/z 641.3165, 479.2633 and 317.2082.

NMR Spectroscopy.

A series of NMR experiments including 1H NMR (FIG. 18), 13C NMR (FIGS. 19 and 20), 1H-1H COSY (FIG. 21), HSQC-DEPT (FIG. 22), HMBC (FIGS. 23 and 24), and 1D-TOCSY were performed to allow assignment of reb M2.

The 1H, 1H-1H COSY, 1H-13C HSQC-DEPT and 1H-13C HMBC NMR data indicated that the central core of the glycoside is a diterpene. The presence of six anomeric protons observed in the 1H and 1H-13C HSQC-DEPT spectra confirm six sugar units in the structure. The methylene 13C resonance at δC 70.9 in the 1H-13C HSQC-DEPT spectrum indicated the presence of a 1→6 sugar linkage in the structure. The linkages of sugar units were assigned using 1H-13C HMBC and 1D-TOCSY correlations.

A HMBC correlation from the methyl protons at δH 1.29 to the carbonyl at δC 181.5 allowed assignment of one of the tertiary methyl groups (C-18) as well as C-19 and provided a starting point for the assignment of the rest of the aglycone. Additional HMBC correlations from the methyl protons (H-18) to carbons at δC 39.8, 43.7, and 59.2 allowed assignment of C3, C4, and C5. Analysis of the 1H-13C HSQC-DEPT data indicated that the carbon at δC 39.8 was a methylene group and the carbon at δC 59.2 was a methine which were assigned as C-3 and C-5, respectively. This left the carbon at δC 43.7, which did not show a correlation in the HSQC-DEPT spectrum, to be assigned as the quaternary carbon, C-4. The 1H chemical shifts for C-3 (δH 1.16 and 2.28) and C-5 (δH 1.24) were assigned using the HSQC-DEPT data. A COSY correlation between one of the H-3 protons (δH 1.16) and a proton at δH 1.49 allowed assignment of one of the H-2 protons which in turn showed a correlation with a proton at δH 0.92 which was assigned to C-1. The remaining 1H and 13C chemical shifts for C-1 and C-2 were then assigned on the basis of additional COSY and HSQC-DEPT correlations and are summarized in the table below.

1H NMR (500 MHz, D2O) and 13C NMR (125 MHz, D2O/TSP) Assignments of the Reb M2 Aglycone

Position 13C 1H 1 41.9 0.92 m 1.93 m 2 21.8 1.49 m 1.86 m 3 39.8 1.16 m 2.28 d (13.4) 4 43.7 — 5 59.2 1.24 d (12.1) 6 24.4 1.73 m 1.94 m 7 44.2 1.49 m 1.56 m 8 46.9 — 9 55.5 1.09 d (7.7) 10 42.4 — 11 22.6 1.66 m 1.70 m 12 39.9 1.60 m 2.00 m 13 90.9 — 14 46.9 1.53 d (12.6) 2.21 d (13.6) 15 49.4 2.15 d (17.2) 2.18 d (18.1) 16 164.0 — 17 107.0 4.98 s 5.16 s 18 31.0 1.29 s 19 181.5 — 20 19.1 0.92 s

The other tertiary methyl singlet, observed at δH 0.92 showed HMBC correlations to C-1 and C-5 and was assigned as C-20. The methyl protons showed additional HMBC correlations to a quaternary carbon (δC 42.4) and a methine (δC 55.5) which were assigned as C-10 and C-9, respectively. COSY correlations between H-5 (δH 1.24) and protons at δH 1.73 and 1.94 then allowed assignment of the H-6 protons which in turn showed correlations to protons at δH 1.49 and 1.56 which were assigned to C-7. The 13C chemical shifts for C-6 (δC 24.4) and C-7 (δC 44.2) were then determined from the HSQC-DEPT data. COSY correlations between H-9 (δH 1.09) and protons at δH 1.66 and 1.70 allowed assignment of the H-11 protons which in turn showed COSY correlations to protons at δH 1.60 and 2.00 which were assigned as the H-12 protons. The HSQC-DEPT data was then used to assign C-11 (δC 22.6) and C-12 (δC 39.9). The olefinic protons observed at δH 4.98 and 5.16 showed HMBC correlations to C-13 (δC 90.9) and were assigned to C-17 (δC 107.0 via HSQC-DEPT). The olefinic protons H-17 showed HMBC correlations to a carbon at δC 49.4 which was assigned as C-15. An additional HMBC correlation from H-9 to a methylene carbon at δC 46.9 then allowed assignment of C-14. The 1H chemical shifts at C-14 (δH 1.53 and 2.21) and C-15 (δH 2.15 and 2.18) were assigned using the HSQC-DEPT data.

A summary of the key HMBC and COSY correlations used to assign the aglycone region are provided below:

Analysis of the 1H-13C HSQC-DEPT data confirmed the presence of six anomeric protons. Three of the anomeric protons were well resolved at δH 5.65 (δC 95.5), 4.92 (δC 104.9), and 4.50 (δC 105.7) in the 1H NMR spectrum. The remaining three anomeric protons observed at δH 4.85 (δC 98.4), 4.84 (δC 105.0), and 4.83 (δC 105.3) were overlapped by the residual solvent resonance in the 1H spectrum. The anomeric proton observed at δH 5.65 showed a HMBC correlation to C-19 which indicated that it corresponds to the anomeric proton of GlcI. Similarly, the anomeric proton observed at δH 4.85 showed a HMBC correlation to C-13 allowing it to be assigned as the anomeric proton of GlcII.

The GlcI anomeric proton (δH 5.65) showed a COSY correlation to a proton at δH 3.96 which was assigned as GlcI H-2 which in turn showed a COSY correlation to a proton at δH 3.89 (GlcI H-3) which showed a COSY correlation with a proton at δH 3.71 (GlcI H-4). Due to data overlap, the COSY spectrum did not allow assignment of the H-5 or H-6 protons. Therefore, a series of 1D-TOCSY experiments were performed using selective irradiation of the GlcI anomeric proton with several different mixing times. In addition to confirming the assignments for GlcI H-2 through H-4, the 1D-TOCSY data showed a proton at δH 3.73 assigned as GlcI H-5 and a proton at δH 4.15 assigned as one of the GlcI H-6 protons. The latter proton was also used for 1D-TOCSY experiments. The selective irradiation of H-6 with several different mixing times also confirmed the assignment of GlcI H-1 to H-5 as well as the remaining methylene proton of H-6 (δH 4.00). Assignment of the 13C chemical shifts for GlcI C-2 (δC 80.5), C-3 (δC 79.0), C-4 (δC 71.5), C-5 (δC 79.0), and C-6 (δC 70.9) was determined using the 1H-13C HSQC-DEPT data to complete the assignment of GlcI. Furthermore, the presence of a methylene 13C resonance at δC 70.9 in the 1H-13C HSQC-DEPT spectrum indicated a 1→6 sugar linkage of GlcI in the structure.

Two of the unassigned glucose moieties were assigned as substituents at C-2 and C-6 of GlcI on the basis of HMBC correlations. The anomeric proton observed at δH 4.83 showed an HMBC correlation to GlcI C-2 and was assigned as the anomeric proton of GlcV. The anomeric proton observed at δH 4.50 showed a HMBC correlation to GlcI C-6 and was assigned as the anomeric proton of GlcVI. The reciprocal HMBC correlations from GlcI H-2 to the anomeric carbon of GlcV and from GlcI H-6 to the anomeric carbon of GlcVI were also observed.

The anomeric proton of GlcV (δH 4.83) showed a COSY correlation with a proton at δH 3.32 which was assigned as GlcV H-2. The GlcV H-2 in turn showed a COSY correlation to a proton at δH 3.51 (GlcV H-3). This latter proton showed an additional correlation with a proton at δH 3.38 (GlcV H-4). H-4 also showed a COSY correlation to a proton at δH 3.55 (GlcV H-5) and GlcV H-5 in turn showed a COSY correlation to GlcV H-6 protons (δH 3.76 and 3.97). Assignment of the 13C chemical shifts for GlcV C-2 (δC 78.5), C-3 (δC 78.7), C-4 (δC 72.9), C-5 (δC 78.8), and C-6 (δC 63.6) was determined using the HSQC-DEPT data. HMBC correlations from GlcV H-3 to C-2 and C-4 and also from GlcV H-4 to C-3 and C-6 confirmed the assignments made above to complete the assignment of GlcV.

Another glucose moiety was assigned as a substituent at C-6 of GlcI on the basis of 1H-13C HSQC-DEPT and HMBC correlations. The relatively downfield shift of a methylene 13C resonance of GlcI at δC 70.9 in the HSQC-DEPT spectrum indicated a 1→6 sugar linkage of GlcI. The anomeric proton observed at δH 4.50 showed a HMBC correlation to GlcI C-6 and was assigned as the anomeric proton of GlcVI. Similarly, methylene protons of Glc1 showed HMBC correlations to the anomeric carbon of GlcVI and this confirmed the presence of a 1→6 sugar linkage between GlcI and GlcVI. The GlcVI anomeric proton showed a COSY correlation to a proton at δH 3.33 which was assigned as GlcVI H-2 which in turn showed a COSY correlation to a proton at δH 3.49 (GlcVI H-3). Due to data overlap, the COSY spectrum did not allow assignment of GlcV H-4 to H-6 based on the COSY correlations. Therefore, a series of 1D-TOCSY experiments were performed using selective irradiation of the GlcVI anomeric proton with different mixing times. In addition to confirming the assignments for GlcVI H-2 through H-3, the 1D-TOCSY data showed protons at δH 3.45 (GlcVI H-4) and δH 3.48 (GlcVI H-5) and protons at δH 3.92 and 3.94 assigned for GlcVI H-6 protons. Assignment of the 13C chemical shifts for GlcVI C-2 (δC 78.1), C-3 (δC 78.6), C-4 (δC 72.3), C-5 (δC 78.8), and C-6 (δC 64.1) was determined using the 1H-13C HSQC-DEPT data to complete the assignment of GlcVI.

A summary of the 1H and 13C chemical shifts for the glycoside at C-19 are found in the table below:

1H NMR (500 MHz, D2O) and 13C NMR (125 MHz, D2O/TSP) Assignments of the Reb M2 Glycoside

Position 13C 1H GlcI-1 95.5 5.65 d (7.6) GlcI-2 80.5 3.96 m GlcI-3 79.0 3.89 m GlcI-4 71.5 3.71 m GlcI-5 79.0 3.73 m GlcI-6 70.9 4.00 m 4.15 d (11.7) GlcV-1 105.3* 4.83* d (8.0) GlcV-2 78.5 3.32 m GlcV-3 78.7 3.51 m GlcV-4 72.9 3.38 m GlcV-5 78.8 3.55 m GlcV-6 63.6 3.76 m 3.97 m GlcVI-1 105.7 4.50 d (7.9) GlcVI-2 78.1 3.33 m GlcVI-3 78.6 3.49 m GlcVI-4 72.3 3.45 m GlcVI-5 78.8 3.48 m GlcVI-6 64.1 3.92 m 3.94 m *1H and 13C values can be exchangeable with GlcIV-1 of the following table.

A summary of the key HMBC, COSY, and 1D-TOCSY correlations used to assign the C-19 glycoside region are provided below:

1H NMR (500 MHz, D2O) and 13C NMR (125 MHz, D2O/TSP) Assignments of the Reb M2 Glycoside

Position 13C# 1H GlcII-1 98.4 4.85 d (7.8) GlcII-2 81.7 3.75 m GlcII-3 88.0 3.98 m GlcII-4 71.3 3.54 m GlcII-5 80.5 3.96 m GlcII-6 63.6 3.45 m 3.77 m GlcIII-1 104.9 4.92 d (7.9) GlcIII-2 76.3 3.32 m GlcIII-3 78.8 3.51 m GlcIII-4 73.3 3.26 t (9.5) GlcIII-5 78.8 3.44 m GlcIII-6 64.4 3.75 m 3.94 m GlcIV-1 105.0 4.84 d (7.8) GlcIV-2 76.1 3.41 m GlcIV-3 78.8 3.46 m GlcIV-4 72.5 3.45 m GlcIV-5 81.7 3.75 m GlcIV-6 65.8 3.55 m 3.78 m

Assignment of GlcII was carried out in a similar manner. The GlcII anomeric proton (δH 4.85) showed a COSY correlation to a proton at δH 3.75 which was assigned as GlcII H-2 which in turn showed a COSY correlation to a proton at δH 3.98 (GlcII H-3). This latter proton showed an additional correlation with a proton at δH 3.54 (GlcII H-4). H-4 also showed a COSY correlation to a proton at δH 3.96 (GlcII H-5). GlcII H-5 also showed a COSY correlation to GlcII H-6 protons (δH 3.77 and 3.45). Assignment of the 13C chemical shifts for GlcII C-2 (δC 81.7), C-3 (δC 88.0), C-4 (δC 71.3), C-5 (δC 80.5), and C-6 (δC 63.6) was determined using the HSQC-DEPT data. HMBC correlations from GlcII H-3 to C-2 and C-4 and also from GlcII H-4 to C-3 and C-6 confirmed the assignments made above to complete the assignment of GlcII.

Two of the remaining unassigned glucose moieties were assigned as substituents at C-2 and C-3 of GlcII on the basis of HMBC correlations. The anomeric proton observed at δH 4.92 showed a HMBC correlation to GlcII C-2 and was assigned as the anomeric proton of GlcIII. The anomeric proton observed at δH 4.84 showed a HMBC correlation to GlcII C-3 and was assigned as the anomeric proton of GlcIV. The reciprocal HMBC correlations between GlcII H-2 and the anomeric carbon of GlcIII and between GlcII H-3 and the anomeric carbon of GlcIV were also observed.

The anomeric proton of GlcIII (δH 4.92) showed a COSY correlation with a proton at δH 3.32 which was assigned as GlcIII H-2. Due to data overlap, the COSY spectrum did not allow assignment of H-3 to H-6 protons. Therefore, a series of 1D-TOCSY experiments were performed using selective irradiation of the GlcIII anomeric proton with different mixing times. In addition to confirming the assignments for GlcIII H-2, the 1D-TOCSY data showed protons at δH 3.51 (GlcIII H-3), δH 3.26 (GlcIII H-4), and δH 3.44 (GlcIII H-5). Once H-4 was assigned using 1D-TOCSY data, COSY correlations from H-4 to H-5 and in turn to H-6 were used to assign H-6. In the COSY spectrum, GlcIII H-4 showed a correlation to GlcIII H-5, which in turn showed COSY correlations to δH 3.94 and 3.75 of GlcIII H-6a and H-6b, respectively. The 13C chemical shifts for GlcIII C-2 (δC 76.3), C-3 (δC 78.8), C-4 (δC 73.3), C-5 (δC 78.8), and C-6 (δC 64.4) were then determined using the 1H-13C HSQC-DEPT correlations to complete the assignment of GlcIII.

The anomeric proton of GlcIV (δH 4.84) which showed a COSY correlation to a proton at δH 3.41 was assigned as GlcIV H-2 which in turn showed a COSY correlation to a proton at δH 3.46 (GlcIV H-3). This latter proton showed an additional correlation with a proton at δH 3.45 (GlcIV H-4) which also showed a COSY correlation to a proton at δH 3.75 (GlcIV H-5). GlcIV H-5 also showed a COSY correlation to GlcIV H-6 protons (δH 3.55 and 3.78). Assignment of the 13C chemical shifts for GlcIV C-2 (δC 76.1), C-3 (δC 78.8), C-4 (δC 72.5), C-5 (δC 81.7), and C-6 (δC 65.8) was determined using the HSQC-DEPT data. HMBC correlations from GlcIV H-3 to C-4 and C-5 and also from GlcIV H-4 to C-3 and C-6 confirmed the assignments made above to complete the assignment of GlcIV.

A summary of the 1H and 13C chemical shifts for the glycoside at C-13 are found in the following table:

1H NMR (500 MHz, D2O) and 13C NMR (125 MHz, D2O/TSP) Assignments of the Reb M2 Glycoside

Position 13C# 1H GlcII-1 98.4 4.85 d (7.8) GlcII-2 81.7 3.75 m GlcII-3 88.0 3.98 m GlcII-4 71.3 3.54 m GlcII-5 80.5 3.96 m GlcII-6 63.6 3.45 m 3.77 m GlcIII-1 104.9 4.92 d (7.9) GlcIII-2 76.3 3.32 m GlcIII-3 78.8 3.51 m GlcIII-4 73.3 3.26 t (9.5) GlcIII-5 78.8 3.44 m GlcIII-6 64.4 3.75 m 3.94 m GlcIV-1 105.0 4.84 d (7.8) GlcIV-2 76.1 3.41 m GlcIV-3 78.8 3.46 m GlcIV-4 72.5 3.45 m GlcIV-5 81.7 3.75 m GlcIV-6 65.8 3.55 m 3.78 m

A summary of the key HMBC, COSY, and 1D-TOCSY correlations used to assign the C-13 glycoside region are provided below:

NMR and MS analyses allowed a full assignment of its structure, shown below. The chemical name of the compound is 13-[(2-O-β-D-glucopyranosyl-3-O-β-D-glucopyranosyl-β-D-glucopyranosyl)oxy] ent-kaur-16-en-19-oic acid-[(2-O-β-D-glucopyranosyl-6-O-β-D-glucopyranosyl-β-D-glucopyranosyl) ester] (rebaudioside M2 or reb M2). The compound is an isomer of rebaudioside M.

Example 41 Directed Evolution of UGT76G1 for the Conversion of Rebaudioside D to Rebaudioside M (Round 2)

The most active clone from the first round of directed evolution of UGT76G1 (see EXAMPLE 26 UGT76G1var94 containing mutations: Q266E_P272A_R334K_G348P_L379G) was chosen as baseline clone for round 2. A list of 53 mutations was established containing different identified positive mutations from the first round and new mutations obtained by DNA2.0 ProteinGPStm strategy. This list of mutations was subsequently used to design 92 variant genes that contained each 3 different mutations. After codon-optimized for expression in E. coli the genes were synthesized, subcloned in the pET30a+ plasmid and used for transformation of E. coli BL21 (DE3) chemically competent cells. The obtained cells were grown in Petri-dishes on solid LB medium in the presence of Kanamycin. Suitable colonies were selected and allowed to grow in liquid LB medium in tubes. Glycerol was added to the suspension as cryoprotectant and 400 μL aliquots were stored at −20° C. and at −80° C.

These storage aliquots of E. coli BL21(DE3) containing the pET30a+_UGT76G1var plasmids were thawed and added to LBGKP medium (20 g/L Luria Broth Lennox; 50 mM PIPES buffer pH 7.00; 50 mM Phosphate buffer pH 7.00; 2.5 g/L glucose and 50 mg/L of Kanamycine). This culture was allowed to shake in a 96 microtiter plate at 30° C. for 8 h.

3.95 mL of production medium containing 60 g/L of Overnight Express™ Instant TB medium (Novagen®), 10 g/L of glycerol and 50 mg/L of Kanamycin was inoculated with 50 μL of above described culture. In a 48 deepwell plate the resulting culture was allowed to stir at 20° C. The cultures gave significant growth and a good OD (600 nm) was obtained. After 44 h, the cells were harvested by centrifugation and frozen.

Lysis was performed by addition of Bugbuster® Master mix (Novagen®) to the thawed cells and the lysate was recovered by centrifugation. Activity tests were performed with 100 μL of fresh lysate that was added to a solution of Rebaudioside D (final concentration 0.5 mM), MgCl2 (final concentration 3 mM) and UDP-Glucose (final concentration 2.5 mM) in 50 mM phosphate buffer pH 7.2.

The reaction was allowed to run at 30° C. and samples were taken after 2, 4, 7 and 24 h. to determine conversion and initial rate by HPLC (CAD detection) using the analytical method that was described above for the transformation of Rebaudioside D to Rebaudioside M. In parallel the experiments were performed with baseline clone, Round1-Var94. The conversion after 22 h. and initial rate for this baseline clone was defined as 100% and the normalized conversions and initial rates for the round 2 clones are depicted in the following table:

Normalized conversion Normalized Reb D to Reb M after initial Clone Mutations* 22h. rate (0-4h) Round1-Var94 UGT76G1 100% 100% (Q266E_P272A_R334K_G348P_L379G) baseline clone Round2-Var1 Round1-Var94 (A213N_P348G_I411V)  70%  86% Round2-Var2 Round1-Var94 (K303G_I423M_Q425E) 120% 134% Round2-Var3 Round1-Var94 (V20L_N138K_S147G)  14%  15% Round2-Var4 Round1-Var94 (I16V_V133A_L299I)  37%  43% Round2-Var5 Round1-Var94 (S241V_S274G_Q432E)  75%  72% Round2-Var6 Round1-Var94 (I16V_L139V_I218V)  62%  68% Round2-Var7 Round1-Var94 (K334R_N409K_Q432E) 104%  92% Round2-Var8 Round1-Var94 (I15L_R141T_I407V)  17%  26% Round2-Var9 Round1-Var94 (R141T_K303G_G379L)  31%  42% Round2-Var10 Round1-Var94 (I190L_K303G_P348G) 131% 149% Round2-Var11 Round1-Var94 (E266Q_F314S_N409R) 106% 132% Round2-Var12 Round1-Var94 (V133A_I295V_K303G)  43%  49% Round2-Var13 Round1-Var94 (I16V_S241V_N409R)  80%  79% Round2-Var14 Round1-Var94 (A239V_K334R_G379L)  58%  55% Round2-Var15 Round1-Var94 (I190L_K393R_V396L) 118% 126% Round2-Var16 Round1-Var94 (L101F_I295M_K393R)  84%  89% Round2-Var17 Round1-Var94 (A239V_E266Q_Q425E)  96% 101% Round2-Var18 Round1-Var94 (V20L_I190L_I423M)  98%  98% Round2-Var19 Round1-Var94 (V20L_G379L_S456L)  84%  81% Round2-Var20 Round1-Var94 (K334R_P348G_N409R)  73%  73% Round2-Var21 Round1-Var94 (E231A_S241V_E449D)  53%  50% Round2-Var22 Round1-Var94 (K188R_L299I_V394I)  56%  59% Round2-Var23 Round1-Var94 (E231A_S274G_V394I) 110% 124% Round2-Var24 Round1-Var94 (S42A_I295V_Q432E)  71%  78% Round2-Var25 Round1-Var94 (A213N_A272P_K334R)  95%  80% Round2-Var26 Round1-Var94 (L158Y_S274K_N409K)  80%  50% Round2-Var27 Round1-Var94 (K188R_I295M_Q425E) 132% 116% Round2-Var28 Round1-Var94 (I15L_I295M_V3941)  53%  36% Round2-Var29 Round1-Var94 (V133A_A239V_V394I)  47%  30% Round2-Var30 Round1-Var94 (L158Y_F314S_K316R)  107%  72% Round2-Var31 Round1-Var94 (L158Y_A239V_A272P)  54%  30% Round2-Var32 Round1-Var94 (F461_D301N_V396L) 109% 101% Round2-Var33 Round1-Var94 (L101F_I218V_Q432E)  78%  54% Round2-Var34 Round1-Var94 (I16V_F46I_I295M) 110%  95% Round2-Var35 Round1-Var94 (A213N_E266S _I407V)  98%  79% Round2-Var36 Round1-Var94 (A239V_S274K_I295M) 102%  89% Round2-Var37 Round1-Var94 (A239V_F314 S_S450K) 105%  99% Round2-Var38 Round1-Var94 (L139V_K188R_D301N)  66%  51% Round2-Var39 Round1-Var94 (I45V_I218V_S274K)  87%  58% Round2-Var40 Round1-Var94 (S241V_K303G_V394I)  78%  57% Round2-Var41 Round1-Var94 (R141T_S274G_K334R)  41%  28% Round2-Var42 Round1-Var94 (V217L_S274G_L299I)  47%  34% Round2-Var43 Round1-Var94 (S274G_D301N_P348G)  98%  91% Round2-Var44 Round1-Var94 (E231A_N409R_S450K)  87%  65% Round2-Var45 Round1-Var94 (R64H_E231A_K316R)  88%  64% Round2-Var46 Round1-Var94 (V394I_N409K_I411V) 110% 100% Round2-Var47 Round1-Var94 (I45V_I295M_K303G) 113%  88% Round2-Var48 Round1-Var94 (L101F_V396L_L398V)  46%  43% Round2-Var49 Round1-Var94 (N27S_L101F_S447A)  54%  37% Round2-Var50 Round1-Var94 (S274G_F314S_L398V) 129% 156% Round2-Var51 Round1-Var94 (E266Q_L299I_K393R)  70%  51% Round2-Var52 Round1-Var94 (V217L_E266S_V394I)  62%  48% Round2-Var53 Round1-Var94 (N138K_A272P_N409R) 118% 102% Round2-Var54 Round1-Var94 (E266S_F314S_Q432E) 124% 146% Round2-Var55 Round1-Var94 (D301N_G379L_L398V)  56%  45% Round2-Var56 Round1-Var94 (F46I_E266S_K334R) 123% 142% Round2-Var57 Round1-Var94 (A272P_V394I_Q432E) 133% 142% Round2-Var58 Round1-Var94 (V394I_I407V_S456L) 118% 114% Round2-Var59 Round1-Var94 (I218V_E266Q_I423M) 106%  98% Round2-Var60 Round1-Var94 (A272P_G379L_I407V)  80%  63% Round2-Var61 Round1-Var94 (E231A_K303G_5456L) 113% 110% Round2-Var62 Round1-Var94 (I190L_E266Q_I407V) 150% 167% Round2-Var63 Round1-Var94 (N27S_L139V_I295V)  43%  25% Round2-Var64 Round1-Var94 (V217L_I423M_S447A)  67%  51% Round2-Var65 Round1-Var94 (L158Y_E266S_E449D)  68%  43% Round2-Var66 Round1-Var94 (S42A_F46I_I407V) 160% 203% Round2-Var67 Round1-Var94 (N138K_E231A_D301N) 118%  93% Round2-Var68 Round1-Var94 (K188R_G379L_N409R)  52%  35% Round2-Var69 Round1-Var94 (I15L_E231A_V396L)  38%  22% Round2-Var70 Round1-Var94 (E231A_Q425E_Q432E) 115% 119% Round2-Var71 Round1-Var94 (D301N_K316R_Q425E) 126% 121% Round2-Var72 Round1-Var94 (L139V_I295M_F314S)  76%  91% Round2-Var73 Round1-Var94 (S147G_E266S_D301N)  30%  18% Round2-Var74 Round1-Var94 (R64H_S147G_S447A)  23%  12% Round2-Var75 Round1-Var94 (S42A_K303G_L398V)  95% 110% Round2-Var76 Round1-Var94 (I45V_D301N_E449D)  62%  60% Round2-Var77 Round1-Var94 (V133A_E266S_I411V)  37%  28% Round2-Var78 Round1-Var94 (I45V_N409R_Q425E)  63%  59% Round2-Var79 Round1-Var94 (R141T_A272P_F314S)  23%  10% Round2-Var80 Round1-Var94 (E2665_S274G_N409R)  81%  91% Round2-Var81 Round1-Var94 (N409K_Q425E_S450K)  81%  84% Round2-Var82 Round1-Var94 (N27S_R64H_K393R)  47%  37% Round2-Var83 Round1-Var94 (S42A_A213N_V217L)  62%  46% Round2-Var84 Round1-Var94 (N275_S274K_I407V)  49%  44% Round2-Var85 Round1-Var94 (I411V_Q425E_S456L)  75%  81% Round2-Var86 Round1-Var94 (A239V_K316R_E449D)  83%  72% Round2-Var87 Round1-Var94 (S147G_A239V_P348G)  18%  7% Round2-Var88 Round1-Var94 (V20L_S274G_S450K)  71%  68% Round2-Var89 Round1-Var94 (F314S_V394I_S447A)  88% 123% Round2-Var90 Round1-Var94 (R64H_E266Q_I295M)  45%  47% Round2-Var91 Round1-Var94 (N138K_I295V_I407V)  50%  51% Round2-Var92 Round1-Var94 (I15L_P348G_Q432E)  18%  13% *Mutations are noted as follows: reference gene-original amino acid-position-new amino acid: For example the mutation of an alanine at position 33 to a glycine for variant 94 from the first round of directed evolution of UGT76G1 is noted as Round1-Var94 (A33G)

Modeling of these results allowed to obtain a ranking of the effect of each mutation. The following mutations were determined as being beneficial for activity: S42A, F46I, I190L, S274G, 1295M, K303G, F314S, K316R, K393R, V394I, I407V, N409K, N409R, Q425E, Q432E, S447A, S456L.

Example 42 In Vivo Production of AtSUS

AtSUS >gi|79328294|ref|NP_001031915.1| sucrose synthase 1 [Arabidopsis thaliana] (SEQ ID NO: 13) MANAERMITRVHSQRERLNETLVSERNEVLALLSRVEAKGKGILQQNQII AEFEALPEQTRKKLEGGPFFDLLKSTQEAIVLPPWVALAVRPRPGVWEYL RVNLHALVVEELQPAEFLHFKEELVDGVKNGNFTLELDFEPFNASIPRPT LHKYIGNGVDFLNRHLSAKLFHDKESLLPLLKFLRLHSHQGKNLMLSEKI QNLNTLQHTLRKAEEYLAELKSETLYEEFEAKFEEIGLERGWGDNAERVL DMIRLLLDLLEAPDPCTLETFLGRVPMVFNVVILSPHGYFAQDNVLGYPD TGGQVVYILDQVRALEIEMLQRIKQQGLNIKPRILILTRLLPDAVGTTCG ERLERVYDSEYCDILRVPFRTEKGIVRKWISRFEVWPYLETYTEDAAVEL SKELNGKPDLIIGNYSDGNLVASLLAHKLGVTQCTIAHALEKTKYPDSDI YWKKLDDKYHFSCQFTADIFAMNHTDFIITSTFQEIAGSKETVGQYESHT AFTLPGLYRVVHGIDVFDPKFNIVSPGADMSIYFPYTEEKRRLTKFHSEI EELLYSDVENKEHLCVLKDKKKPILFTMARLDRVKNLSGLVEWYGKNTRL RELANLVVVGGDRRKESKDNEEKAEMKKMYDLIEEYKLNGQFRWISSQMD RVRNGELYRYICDTKGAFVQPALYEAFGLTVVEAMTCGLPTFATCKGGPA EIIVHGKSGFHIDPYHGDQAADTLADFFTKCKEDPSHWDEISKGGLQRIE EKYTWQIYSQRLLTLTGVYGFWKHVSNLDRLEARRYLEMFYALKYRPLAQ AVPLAQDD.

The synthetic gene of AtSuS that was codon optimized for expression in E. coli and subcloned in the pET30a+ plasmid using the NdeI and XhoI restriction sites. The pET30A+ vector containing the AtSUS gene was used to transform electrocompetent E. coli B121(DE3) cells. The obtained cells were grown in petri-dishes in the presence of Kanamycin and suitable colonies were selected and allowed to grow in liquid LB medium (erlenmeyer flasks). Glycerol was added to the suspension as cryoprotectant and 400 μL aliquots were stored at −20° C. and at −80° C.

The storage aliquots of E. coli BL21(DE3) containing the pET30A+_AtSUS plasmids were thawed and added to 30 mL of LBGKP medium (20 g/L Luria Broth Lennox; 50 mM PIPES buffer pH 7.00; 50 mM Phosphate buffer pH 7.00; 2.5 g/L glucose and 50 mg/L of Kanamycine). This culture was allowed to shake at 135 rpm at 30° C. for 8 h.

The production medium contained 60 g/L of overnight express instant TB medium (Novagen), 10 g/L of glycerol and 50 mg/L of Kanamycine. The preculture was added to 800 mL of this medium and the solution was allowed to stir at 20° C. while taking samples to measure the OD and pH. The culture gave significant growth and a good OD was obtained. After 40 h, the cells were harvested by centrifugation and frozen to obtain 30.1 g of cell wet weight.

Lysis was performed by Fastprep (MP Biomedicals, Lysing matrix B, speed 6.0, 3×40 sec) with a cell suspension of 200 mg of cells in 1.0 mL of 50 mM Tris buffer pH 7.5. The lysate was recovered by centrifugation and used fresh.

Example 43 Conversion of Rebaudioside A to Rebaudioside M with In Situ Prepared UDP-Glucose Using UGTSL2, UGT76G1-R1-F12 and AtSUS

The reaction was performed at 1 mL scale using 100 mM of sucrose, 3 mM of MgCl2, 0.25 mM of UDP and 0.5 mM of Rebaudioside A in potassium phosphate buffer (50 mM final concentration, pH 7.5). The reaction was started by adding 15 μL of UGTSL2 (see EXAMPLE 27) lysate (2 U/mL), 150 μL of UGT76G1var94 (see EXAMPLE 26) (2.5 U/mL) and 15 μL of AtSUS (see EXAMPLE 42) (400 U/mL). The reaction was followed by HPLC after quenching 125 μL samples with 10 μL of 2 N H2SO4 and 115 μL of 60% methanol. 68% of Rebaudioside M and 26% of Rebaudioside M2 were obtained after 21 h of reaction time.

Claims

1. A method for producing target steviol glycosides, comprising the steps of:

a. providing a starting composition comprising an organic compound with at least one carbon atom;
b. providing a microorganism or a biocatalyst containing at least one enzyme selected from steviol biosynthesis enzymes, UDP-glycosyltransferases, and optionally providing UDP-glucose recycling enzymes;
c. contacting the microorganism with a medium containing the starting composition to produce a medium comprising at least one target steviol glycoside.

2. (canceled)

3. The method of claim 1, further comprising the step of:

d. purifying the target steviol glycoside from the medium to provide a highly purified target steviol glycoside composition.

4. The method of claim 1, wherein the organic compound is selected from the group consisting of polyols, carbohydrates, steviol glycosides and combinations thereof.

5. (canceled)

6. (canceled)

7. (canceled)

8. The method of claim 1, wherein the biocatalyst is an enzyme, or a cell comprising one or more enzymes, capable of converting the organic compound to target steviol glycoside.

9. The method of claim 1, wherein the target steviol glycoside is selected from the group consisting of stevioside, reb A, reb D, reb D2, reb E, reb M, reb M2 and mixtures thereof.

10. The method of claim 1, wherein the enzyme is selected from the group consisting of geranylgeranyl diphosphate synthase, copalyl diphosphate synthase, kaurene synthase, kaurene oxidase, kaurenoic acid 13-hydroxylase (KAH), steviol synthetase, deoxyxylulose 5-phosphate synthase (DXS), D-1-deoxyxylulose 5-phosphate reductoisomerase (DXR), 4-diphosphocytidyl-2-C-methyl-D-erythritol synthase (CMS), 4-diphosphocytidyl-2-C-methyl-D-erythritol kinase (CMK), 4-diphosphocytidyl-2-Cmethyl-D-erythritol 2,4-cyclodiphosphate synthase (MCS), 1-hydroxy-2-methyl-2(E)butenyl 4-diphosphate synthase (HDS), 1-hydroxy-2-methyl-2(E)-butenyl 4-diphosphate reductase (HDR), acetoacetyl-CoA thiolase, truncated HMG-CoA reductase, mevalonate kinase, phosphomevalonate kinase, mevalonate pyrophosphate decarboxylase, cytochrome P450 reductase, UGT91D2, UGTSL2, UGT76G1, or UGT76G1 containing one or more point mutations selected from S42A, F46I, I190L, S274G, I295M, K303G, F314S, K316R, K393R, V394I, I407V, N409K, N409R, Q425E, Q432E, S447A and S456L.

11. The method of claim 3, wherein the highly purified target steviol glycoside composition has a target steviol glycoside purity greater than about 95% by weight on a dry basis.

12. (canceled)

13. (canceled)

14. The method of claim 11, wherein the target steviol glycoside is reb M.

15. The method of claim 3, wherein the target steviol glycoside is polymorphic.

16. (canceled)

17. (canceled)

18. (canceled)

19. (canceled)

20. Isolated and highly purified reb D2 having the following structure:

21. (canceled)

22. (canceled)

23. (canceled)

24. The method of claim 1, wherein the method comprises:

a. contacting a starting composition comprising reb A with an enzyme selected from the group of enzymes capable of transforming reb A to reb D2, UDP glucose, and optionally UDP-glucose recycling enzymes to produce a composition comprising reb D2; and
b. isolating, and optionally, purifying the composition comprising reb D2.

25. The method of claim 24, wherein reb D2 has a purity greater than about 95% by weight on an anhydrous basis.

26. Isolated and highly purified reb M2 having the following structure:

27. A consumable product comprising isolated and highly purified reb M2 or highly purified reb D2.

28. (canceled)

29. The consumable product of claim 27, wherein the product is a beverage.

30. The method of claim 1, wherein the method comprises:

a. contacting a starting composition comprising reb D2 with an enzyme selected from the group consisting of enzymes capable of transforming reb D2 to reb M2, UDP-glucose, and optionally UDP-glucose recycling enzymes to produce a composition comprising reb M2; and
b. isolating, and optionally, purifying the composition comprising reb M2.

31. The method of claim 30, wherein reb M2 has a purity greater than about 95% by weight on an anhydrous basis.

32. (canceled)

33. The consumable product of claim 27, further comprising at least one functional ingredient selected from the group consisting of saponins, antioxidants, dietary fiber sources, fatty acids, vitamins, glucosamine, minerals, preservatives, hydration agents, probiotics, prebiotics, weight management agents, osteoporosis management agents, phytoestrogens, long chain primary aliphatic saturated alcohols, phytosterols and combinations thereof.

34. The consumable product of claim 27, further comprising a compound selected from the group consisting of stevia, stevia extract, steviolmonoside, steviolbioside, rubusoside, dulcoside A, dulcoside B, rebaudioside B, rebaudioside G, stevioside, rebaudioside C, rebaudioside F, rebaudioside A, rebaudioside I, rebaudioside E, rebaudioside H, rebaudioside L, rebaudioside K, rebaudioside J, rebaudioside M, rebaudioside M2, rebaudioside D, rebaudioside D2, rebaudioside Nor rebaudioside 0, or other glycoside of steviol found in Stevia rebaudiana, mogrosides, brazzein, neohesperidin dihydrochalcone, glycyrrhizic acid and its salts, thaumatin, perillartine, pemandulcin, mukuroziosides, baiyunoside, phlomisoside-I, dimethyl-hexahydrofluorene-dicarboxylic acid, abrusosides, periandrin, camosiflosides, cyclocarioside, pterocaryosides, polypodoside A, brazilin, hemandulcin, phillodulcin, glycyphyllin, phlorizin, trilobatin, dihydroflavonol, dihydroquercetin-3-acetate, neoastilibin, trans-cinnamaldehyde, monatin and its salts, selligueain A, hematoxylin, monellin, osladin, pterocaryoside A, pterocaryoside B, mabinlin, pentadin, miraculin, curculin, neoculin, chlorogenic acid, cynarin, Luo Han Guo sweetener, mogroside V, mogroside VI, grosmomomside, siamenoside, NSF-02, NSF-03, NSF-04, allulose, allose, D-tagatose, erythritol and combinations thereof.

35. The consumable product of claim 27 wherein the product is a tabletop sweetener composition comprising isolated and purified reb D2 or isolated and purified reb M2.

36. The consumable product of claim 27, further comprising at least one additive selected from the group consisting of carbohydrates, polyols, amino acids and their corresponding salts, poly-amino acids and their corresponding salts, sugar acids and their corresponding salts, nucleotides, organic acids, inorganic acids, organic salts including organic acid salts and organic base salts, inorganic salts, bitter compounds, flavorants and flavoring ingredients, astringent compounds, proteins or protein hydrolysates, surfactants, emulsifiers, flavonoids, alcohols, polymers and combinations thereof.

37. (canceled)

38. (canceled)

39. (canceled)

40. A method for enhancing the sweetness of a beverage comprising a sweetener comprising:

a.) providing a beverage comprising a sweetener; and
b.) adding a sweetness enhancer selected from reb D2, reb M2 or a combination thereof, wherein reb D2 and/or reb M2 1s present m a concentration at or below the sweetness recognition threshold.
Patent History
Publication number: 20160198748
Type: Application
Filed: May 28, 2014
Publication Date: Jul 14, 2016
Inventors: Indra Prakash (Alpharetta, GA), Cynthia Bunders (Atlanta, GA), Pankaj Soni (Kennesaw, GA), Avetik Markosyan (Kuala Lumpur), Jarrin Cyrille (Muret), Aurelien Badie (Labege), Rober Ter Halle (Baziege)
Application Number: 14/894,084
Classifications
International Classification: A23L 1/236 (20060101); A23L 2/60 (20060101); C07H 15/256 (20060101); C12P 19/56 (20060101);