US20160198748A1

US20160198748A1 - High-Purity Steviol Glycosides

Info

Publication number: US20160198748A1
Application number: US14/894,084
Authority: US
Inventors: Indra Prakash; Cynthia Bunders; Pankaj SONI; Avetik Markosyan; Jarrin CYRILLE; Aurelien Badie; Rober Ter Halle
Original assignee: PureCircle Sdn Bhd; Coca Cola Co
Current assignee: PureCircle Sdn Bhd
Priority date: 2013-05-28
Filing date: 2014-05-28
Publication date: 2016-07-14
Also published as: MX2019005688A; BR112015030082A2; US9752174B2; CN105408339A; CA3089783C; CA2913252C; CN112626154A; US10683526B2; WO2014193888A1; US20190040434A1; US20140357588A1; BR112015029684B1; EP3004127A1; MX2015016096A; MX2015016362A; EP3004128A1; WO2014193934A1; US20180100175A1; CA2913252A1; CN105492453B

Abstract

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.

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]_D ²⁵−19.0° 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 H₂SO₄and 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 H₂SO₄and 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 H₂SO₄and 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 MgCl₂in 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 MgCl₂in 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 MgCl₂in 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 H₂SO₄and 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 MgCl₂in 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 MgCl₂in 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 MgCl₂in 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 MgCl₂in 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 MgCl₂in 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 MgCl₂in 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 MgCl₂in 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 MgCl₂in 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 C₅D₅N^a-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

^aassignments made on the basis of COSY, HMQC and HMBC correlations;
^bChemical shift values are in δ (ppm);
^cCoupling 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-d₅and 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 (δ_H8.74 and δ_C150.35 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 δ_H5.04 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 δ_C69.9 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 δ_H1.29 to the carbonyl at δ_C177.7 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 δ_C38.9, 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 δ_C38.9 was a methylene group and the carbon at δ_C57.8 was a methine which were assigned as C-3 and C-5, respectively. This left the carbon at δ_C45.0, 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 (δ_H0.98 and 2j.36) and C-5 (δ_H1.04) were assigned using the HSQC-DEPT data. A COSY correlation between one of the H-3 protons (δ_H0.98) and a proton at δ_H1.43 allowed assignment of one of the H-2 protons which in turn showed a correlation with a proton at δ_H0.75 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 δ_H1.30 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 (δ_C40.3) and a methine carbon (δ_C54.5) which were assigned as C-10 and C-9, respectively. COSY correlations between H-5 (δ_H1.04) and protons at δ_H1.92 and 2.43 then allowed assignment of the H-6 protons which in turn showed correlations to protons at δ_H1.22 and 1.30 which were assigned to C-7. The ¹³C chemical shifts for C-6 (δ_C22.7) and C-7 (δ_C42.2) were then determined from the HSQC-DEPT data. COSY correlations between H-9 (δ_H0.88) and protons at δ_H1.65 and 1.69 allowed assignment of the H-11 protons which in turn showed COSY correlations to protons at δ_H1.99 and 2.25 which were assigned as the H-12 protons. The HSQC-DEPT data was then used to assign C-11 (δ_C21.1) and C-12 (δ_C37.5). HMBC correlations from the H-12 proton (δ_H2.25) to carbons at δ_C87.1 and 154.7 allowed assignment of C-13 and C-16, respectively. The olefinic protons observed at δ_H5.01 and 5.64 showed HMBC correlations to C-13 and were assigned to C-17 (δ_C105.2 via HSQC-DEPT). The olefinic protons H-17 and the methine proton H-9 showed HMBC correlations to a carbon at δ_C48.3 which was assigned as C-15. An additional HMBC correlation from H-9 to a methylene carbon at δ_C44.5 then allowed assignment of C-14. The ¹H chemical shifts at C-14 (δ_H1.80 and 2.65) and C-15 (δ_H1.31 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 δ_H6.02 (δ_C96.1), 5.57 (δ_C105.3), and 5.34 (δ_C105.3) in the ¹H NMR spectrum. The remaining two anomeric protons observed at δ_H5.04 (δ_C105.6) and 5.07 (δ_C98.7) which were obscured by solvent (HOD) resonance in the ¹H spectrum were identified by ¹H-¹³C HSQC-DEPT data. The anomeric proton observed at δ_H6.02 showed HMBC correlation to C-19 which indicated that it corresponds to the anomeric proton of Glc_I. Similarly, the anomeric proton observed at δ_H5.07 showed an HMBC correlation to C-13 allowing it to be assigned as the anomeric proton of Glc_II.
The Glc_Ianomeric proton (δ_H6.02) showed a COSY correlation to a proton at δ_H4.07 was assigned as Glc_IH-2 which in turn showed a COSY correlation to a proton at δ_H4.22 (Glc_IH-3) which showed a COSY correlation with a proton at δ_H4.12 (Glc_IH-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 Glc_Ianomeric proton with several different mixing times. In addition to confirming the assignments for Glc_IH-2 through H-4, the 1D-TOCSY data showed a proton at δ_H4.04 assigned as Glc_IH-5 and a proton at δ_H4.68 assigned as one of the Glc_IH-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 Glc_IH-1 to H-5 as well as the remaining methylene proton of H-6 (δ_H4.30). Assignment of the ¹³C chemical shifts for Glc_IC-2 (δ_C74.2), C-3 (δ_C79.1), C-4 (δ_C72.1), C-5 (δ_C78.5), and C-6 (δ_C69.9) was determined using the ¹H-¹³C HSQC-DEPT data to complete the assignment of Glc_I. Furthermore, the presence of a methylene ¹³C resonance at δ_C69.9 in the ¹H-¹³C HSQC-DEPT spectrum indicated a 1→6 sugar linkage of Glc_Iin the structure.
Out of four remaining unassigned glucose moieties, one was assigned as a substituent at C-6 of Glc_Ion the basis of ¹H-¹³C HSQC-DEPT, HMBC, and 1D-TOCSY correlations. The relatively downfield shift of a methylene ¹³C resonance of Glc_Iat δ_C69.9 in the HSQC-DEPT spectrum indicated a 1→6 sugar linkage of Glc_I. The anomeric proton observed at δ_H5.04 showed HMBC correlation to Glc_IC-6 and was assigned as the anomeric proton of Glc_V. Similarly, methylene protons of Glc_Ishowed HMBC correlations to anomeric carbon of Glc_Vconfirming the presence of a 1→6 sugar linkage between Glc_Iand Glc_V. The Glc_Vanomeric proton showed a COSY correlation to a proton at δ_H4.00 which was assigned as Glc_VH-2 which in turn showed a COSY correlation to a proton at δ_H4.22 (Glc_VH-3). Due to data overlap, the COSY spectrum did not allow assignment of Glc_VH-4 based on the COSY correlation of Glc_VH-3. However, in the HMBC spectrum, Glc_VH-3 showed a correlation to Glc_VC-5 (δ_C78.9). In HSQC-DEPT spectrum, Glc_VC-5 showed a correlation to δ_H3.89 (Glc_VH-5). The Glc_VH-5 showed COSY correlations to δ_H4.21, 4.37, and 4.48. In the HSQC-DEPT spectrum, δ_H4.21 showed a correlation to δ_C71.4 (Glc_VH-4), while δ_H4.37 and 4.48 showed a correlation to δ_C63.1 and were assigned to Glc_VH-6a and H-6b, respectively. Assignment of the ¹³C chemical shifts for Glc_VC-2 (δ_C75.7) and C-3 (δ_C79.1) was determined using the ¹H-¹³C HSQC-DEPT data to complete the assignment of Glc_V.
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

Glc_I-1	96.1	6.02 d (8.1)
Glc_I-2	74.2	4.07 m
Glc_I-3	79.1^#	4.22 m^#
Glc_I-4	72.1	4.12 m
Glc_I-5	78.5	4.04 m
Glc_I-6	69.9	4.30 m
		4.68 d (10.7)
Glc_V-1	105.6	5.04 (8.1)
Glc_V-2	75.7	4.00 m
Glc_V-3	79.1^#	4.22 m^#
Glc_V-4	71.4	4.21 m
Glc_V-5	78.9	3.89 m
Glc_V-6	63.1	4.37 m
		4.48 m

¹H and ¹³C values can be exchangeable between positions Glc₁-3, Glc_V-3and Glc_IV-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 Glc_IIwas carried out in a similar manner. The Glc_IIanomeric proton (δ_H5.07) showed a COSY correlation to a proton at δ_H4.37, assigned as Glc_IIH-2, which in turn showed a COSY correlation to a proton at δ_H4.18 (Glc_IIH-3). This latter proton showed an additional correlation with a proton at δ_H3.88 (Glc_IIH-4) which also showed a COSY correlation to a proton at δ_H3.79 (Glc_IIH-5). Glc_IIH-5 also showed a COSY correlation to Glc_IIH-6 protons (δ_H4.08 and 4.46). Assignment of the ¹³C chemical shifts for Glc_IIC-2 (δ_C81.3), C-3 (δ_C88.4), C-4 (δ_C71.1), C-5 (δ_C77.9), and C-6 (δ_C63.2) was determined using the HSQC-DEPT data. HMBC correlations from Glc_IIH-3 to C-2 and C-4 and also from Glc_IIH-4 to C-2 and C-5 confirmed the assignments made above. Additional HMBC correlations of Glc_IIH-4 to Glc_IIC-6 further support to complete the assignment of Glc_II.
Two of the remaining unassigned glucose moieties were assigned as substituents at C-2 and C-3 of Glc_IIon the basis of HMBC correlations. The anomeric proton observed at δ_H5.57 showed a HMBC correlation to Glc_IIC-2 and was assigned as the anomeric proton of Glc_III. The anomeric proton observed at δ_H5.34 showed a HMBC correlation to Glc_IIC-3 and was assigned as the anomeric proton of Glc_IV. The reciprocal HMBC correlations from Glc_IIH-2 to the anomeric carbon of Glc_IIIand from Glc_IIH-3 to the anomeric carbon of Glc_IVwere also observed.
The anomeric proton of Glc_III(δ_H5.57) showed a COSY correlation with a proton at δ_H4.19 which was assigned as Glc_IIIH-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 Glc_IIIanomeric proton with several different mixing times. In addition to confirming the assignments for Glc_IIIH-2, the 1D-TOCSY data showed protons at δ_H4.24 (Glc_IIIH-3), δ_H4.27 (Glc_IIIH-4), and δ_H3.94 (Glc_IIIH-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, Glc_IIIH-4 showed a correlation to Glc_IIIH-5, which in turn showed COSY correlations to δ_H4.41 and 4.50 of Glc_IIIH-6a and H-6b, respectively. The ¹³C chemical shifts for Glc_IIIC-2 (δ_C76.8), C-3 (δ_C78.9), C-4 (δ_C72.4), C-5 (δ_C78.8), and C-6 (δ_C63.5) were then determined using the ¹H-¹³C HSQC-DEPT correlations to complete the assignment of Glc_III.
The anomeric proton of Glc_IV(δ_H5.34) showed a COSY correlation with a proton at δ_H4.06 which was assigned as Glc_IVH-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 Glc_IVanomeric proton with several different mixing times. In addition to confirming the assignments for Glc_IVH-2, the 1D-TOCSY data showed protons at δ_H4.22 (Glc_IVH-3), δ_H4.18 (Glc_IVH-4), and δ_H4.10 (Glc_IVH-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, Glc_IVH-4 showed a correlation to Glc_IVH-5, which in turn showed COSY correlations to δ_H4.32 and 4.58, Glc_IVH-6a and H-6b, respectively. The ¹³C chemical shifts for Glc_IVC-2 (δ_C75.8), C-3 (δ_C78.9), C-4 (δ_C72.0), C-5 (δ_C79.3), and C-6 (δ_C62.9) were then determined using the ¹H-¹³C HSQC-DEPT correlations to complete the assignment of Glc_IV.
The large coupling constants observed for the anomeric protons of the glucose moieties at δ_H6.02 (d, J=8.1 Hz), 5.57 (d, J=7.6 Hz), 5.34 (d, J=7.9 Hz) and δ_H5.04 (d, J=8.1 Hz), suggested their β-orientation. While the remaining anomeric proton at δ_H5.07 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

Glc_II-1	98.7	5.07 (~8)*
Glc_II-2	81.3	4.37 m
Glc_II-3	88.4	4.18 m
Glc_II-4	71.1	3.88 m
Glc_II-5	77.9	3.79 m
Glc_II-6	63.2	4.08 m
		4.47 m
Glc_III-1	105.3	5.57 d (7.6)
Glc_III-2	76.8	4.19 m
Glc_III-3	78.9	4.24 m
Glc_III-4	72.4	4.27 m
Glc_III-5	78.8	3.94 m
Glc_III-6	63.5	4.41 m
		4.50 m
Glc_IV-1	105.3	5.34 d (7.9)
Glc_IV-2	75.8	4.06 m
Glc_IV-3	78.9^#	4.22 m^#
Glc_IV-4	72.0	4.18 m
Glc_IV-5	79.3	4.10 m
Glc_IV-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, Glc_V-3and Glc_IV-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

Gradient:

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.

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 (δ_H4.79 ppm) and TSP (δ_C0.00 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 δ_C70.9 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 δ_H1.29 to the carbonyl at δ_C181.5 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 δ_C39.8, 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 δ_C39.8 was a methylene group and the carbon at δ_C59.2 was a methine which were assigned as C-3 and C-5, respectively. This left the carbon at δ_C43.7, 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 (δ_H1.16 and 2.28) and C-5 (δ_H1.24) were assigned using the HSQC-DEPT data. A COSY correlation between one of the H-3 protons (δ_H1.16) and a proton at δ_H1.49 allowed assignment of one of the H-2 protons which in turn showed a correlation with a proton at δ_H0.92 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 δ_H0.92 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 (δ_C42.4) and a methine (δ_C55.5) which were assigned as C-10 and C-9, respectively. COSY correlations between H-5 (δ_H1.24) and protons at δ_H1.73 and 1.94 then allowed assignment of the H-6 protons which in turn showed correlations to protons at δ_H1.49 and 1.56 which were assigned to C-7. The ¹³C chemical shifts for C-6 (δ_C24.4) and C-7 (δ_C44.2) were then determined from the HSQC-DEPT data. COSY correlations between H-9 (δ_H1.09) and protons at δ_H1.66 and 1.70 allowed assignment of the H-11 protons which in turn showed COSY correlations to protons at δ_H1.60 and 2.00 which were assigned as the H-12 protons. The HSQC-DEPT data was then used to assign C-11 (δ_C22.6) and C-12 (δ_C39.9). The olefinic protons observed at δ_H4.98 and 5.16 showed HMBC correlations to C-13 (δ_C90.9) and were assigned to C-17 (δ_C107.0 via HSQC-DEPT). The olefinic protons H-17 showed HMBC correlations to a carbon at δ_C49.4 which was assigned as C-15. An additional HMBC correlation from H-9 to a methylene carbon at δ_C46.9 then allowed assignment of C-14. The ¹H chemical shifts at C-14 (δ_H1.53 and 2.21) and C-15 (δ_H2.15 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 δ_H5.65 (δ_C95.5), 4.92 (δ_C104.9), and 4.50 (δ_C105.7) in the ¹H NMR spectrum. The remaining three anomeric protons observed at δ_H4.85 (δ_C98.4), 4.84 (δ_C105.0), and 4.83 (δ_C105.3) were overlapped by the residual solvent resonance in the ¹H spectrum. The anomeric proton observed at δ_H5.65 showed a HMBC correlation to C-19 which indicated that it corresponds to the anomeric proton of Glc_I. Similarly, the anomeric proton observed at δ_H4.85 showed a HMBC correlation to C-13 allowing it to be assigned as the anomeric proton of Glc_II.
The Glc_Ianomeric proton (δ_H5.65) showed a COSY correlation to a proton at δ_H3.96 which was assigned as Glc_IH-2 which in turn showed a COSY correlation to a proton at δ_H3.89 (Glc_IH-3) which showed a COSY correlation with a proton at δ_H3.71 (Glc_IH-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 Glc_Ianomeric proton with several different mixing times. In addition to confirming the assignments for Glc_IH-2 through H-4, the 1D-TOCSY data showed a proton at δ_H3.73 assigned as Glc_IH-5 and a proton at δ_H4.15 assigned as one of the Glc_IH-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 Glc_IH-1 to H-5 as well as the remaining methylene proton of H-6 (δ_H4.00). Assignment of the ¹³C chemical shifts for Glc_IC-2 (δ_C80.5), C-3 (δ_C79.0), C-4 (δ_C71.5), C-5 (δ_C79.0), and C-6 (δ_C70.9) was determined using the ¹H-¹³C HSQC-DEPT data to complete the assignment of Glc_I. Furthermore, the presence of a methylene ¹³C resonance at δ_C70.9 in the ¹H-¹³C HSQC-DEPT spectrum indicated a 1→6 sugar linkage of Glc_Iin the structure.
Two of the unassigned glucose moieties were assigned as substituents at C-2 and C-6 of Glc_Ion the basis of HMBC correlations. The anomeric proton observed at δ_H4.83 showed an HMBC correlation to Glc_IC-2 and was assigned as the anomeric proton of Glc_V. The anomeric proton observed at δ_H4.50 showed a HMBC correlation to Glc_IC-6 and was assigned as the anomeric proton of Glc_VI. The reciprocal HMBC correlations from Glc_IH-2 to the anomeric carbon of Glc_Vand from Glc_IH-6 to the anomeric carbon of Glc_VIwere also observed.
The anomeric proton of Glc_V(δ_H4.83) showed a COSY correlation with a proton at δ_H3.32 which was assigned as Glc_VH-2. The Glc_VH-2 in turn showed a COSY correlation to a proton at δ_H3.51 (Glc_VH-3). This latter proton showed an additional correlation with a proton at δ_H3.38 (Glc_VH-4). H-4 also showed a COSY correlation to a proton at δ_H3.55 (Glc_VH-5) and Glc_VH-5 in turn showed a COSY correlation to Glc_VH-6 protons (δ_H3.76 and 3.97). Assignment of the ¹³C chemical shifts for Glc_VC-2 (δ_C78.5), C-3 (δ_C78.7), C-4 (δ_C72.9), C-5 (δ_C78.8), and C-6 (δ_C63.6) was determined using the HSQC-DEPT data. HMBC correlations from Glc_VH-3 to C-2 and C-4 and also from Glc_VH-4 to C-3 and C-6 confirmed the assignments made above to complete the assignment of Glc_V.
Another glucose moiety was assigned as a substituent at C-6 of Glc_Ion the basis of ¹H-¹³C HSQC-DEPT and HMBC correlations. The relatively downfield shift of a methylene ¹³C resonance of Glc_Iat δ_C70.9 in the HSQC-DEPT spectrum indicated a 1→6 sugar linkage of Glc_I. The anomeric proton observed at δ_H4.50 showed a HMBC correlation to Glc_IC-6 and was assigned as the anomeric proton of Glc_VI. Similarly, methylene protons of Glc₁showed HMBC correlations to the anomeric carbon of Glc_VIand this confirmed the presence of a 1→6 sugar linkage between Glc_Iand Glc_VI. The Glc_VIanomeric proton showed a COSY correlation to a proton at δ_H3.33 which was assigned as Glc_VIH-2 which in turn showed a COSY correlation to a proton at δ_H3.49 (Glc_VIH-3). Due to data overlap, the COSY spectrum did not allow assignment of Glc_VH-4 to H-6 based on the COSY correlations. Therefore, a series of 1D-TOCSY experiments were performed using selective irradiation of the Glc_VIanomeric proton with different mixing times. In addition to confirming the assignments for Glc_VIH-2 through H-3, the 1D-TOCSY data showed protons at δ_H3.45 (Glc_VIH-4) and δ_H3.48 (Glc_VIH-5) and protons at δ_H3.92 and 3.94 assigned for Glc_VIH-6 protons. Assignment of the ¹³C chemical shifts for Glc_VIC-2 (δ_C78.1), C-3 (δ_C78.6), C-4 (δ_C72.3), C-5 (δ_C78.8), and C-6 (δ_C64.1) was determined using the ¹H-¹³C HSQC-DEPT data to complete the assignment of Glc_VI.
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

Glc_I-1	95.5	5.65 d (7.6)
Glc_I-2	80.5	3.96 m
Glc_I-3	79.0	3.89 m
Glc_I-4	71.5	3.71 m
Glc_I-5	79.0	3.73 m
Glc_I-6	70.9	4.00 m
		4.15 d (11.7)
Glc_V-1	105.3*	4.83* d (8.0)
Glc_V-2	78.5	3.32 m
Glc_V-3	78.7	3.51 m
Glc_V-4	72.9	3.38 m
Glc_V-5	78.8	3.55 m
Glc_V-6	63.6	3.76 m
		3.97 m
Glc_VI-1	105.7	4.50 d (7.9)
Glc_VI-2	78.1	3.33 m
Glc_VI-3	78.6	3.49 m
Glc_VI-4	72.3	3.45 m
Glc_VI-5	78.8	3.48 m
Glc_VI-6	64.1	3.92 m
		3.94 m

*¹H and ¹³C values can be exchangeable with Glc_IV-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:


Position	¹³C^#	¹H

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

Assignment of Glc_IIwas carried out in a similar manner. The Glc_IIanomeric proton (δ_H4.85) showed a COSY correlation to a proton at δ_H3.75 which was assigned as Glc_IIH-2 which in turn showed a COSY correlation to a proton at δ_H3.98 (Glc_IIH-3). This latter proton showed an additional correlation with a proton at δ_H3.54 (Glc_IIH-4). H-4 also showed a COSY correlation to a proton at δ_H3.96 (Glc_IIH-5). Glc_IIH-5 also showed a COSY correlation to Glc_IIH-6 protons (δ_H3.77 and 3.45). Assignment of the ¹³C chemical shifts for Glc_IIC-2 (δ_C81.7), C-3 (δ_C88.0), C-4 (δ_C71.3), C-5 (δ_C80.5), and C-6 (δ_C63.6) was determined using the HSQC-DEPT data. HMBC correlations from Glc_IIH-3 to C-2 and C-4 and also from Glc_IIH-4 to C-3 and C-6 confirmed the assignments made above to complete the assignment of Glc_II.
Two of the remaining unassigned glucose moieties were assigned as substituents at C-2 and C-3 of Glc_IIon the basis of HMBC correlations. The anomeric proton observed at δ_H4.92 showed a HMBC correlation to Glc_IIC-2 and was assigned as the anomeric proton of Glc_III. The anomeric proton observed at δ_H4.84 showed a HMBC correlation to Glc_IIC-3 and was assigned as the anomeric proton of Glc_IV. The reciprocal HMBC correlations between Glc_IIH-2 and the anomeric carbon of Glc_IIIand between Glc_IIH-3 and the anomeric carbon of Glc_IVwere also observed.
The anomeric proton of Glc_III(δ_H4.92) showed a COSY correlation with a proton at δ_H3.32 which was assigned as Glc_IIIH-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 Glc_IIIanomeric proton with different mixing times. In addition to confirming the assignments for Glc_IIIH-2, the 1D-TOCSY data showed protons at δ_H3.51 (Glc_IIIH-3), δ_H3.26 (Glc_IIIH-4), and δ_H3.44 (Glc_IIIH-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, Glc_IIIH-4 showed a correlation to Glc_IIIH-5, which in turn showed COSY correlations to δ_H3.94 and 3.75 of Glc_IIIH-6a and H-6b, respectively. The ¹³C chemical shifts for Glc_IIIC-2 (δ_C76.3), C-3 (δ_C78.8), C-4 (δ_C73.3), C-5 (δ_C78.8), and C-6 (δ_C64.4) were then determined using the ¹H-¹³C HSQC-DEPT correlations to complete the assignment of Glc_III.
The anomeric proton of Glc_IV(δ_H4.84) which showed a COSY correlation to a proton at δ_H3.41 was assigned as Glc_IVH-2 which in turn showed a COSY correlation to a proton at δ_H3.46 (Glc_IVH-3). This latter proton showed an additional correlation with a proton at δ_H3.45 (Glc_IVH-4) which also showed a COSY correlation to a proton at δ_H3.75 (Glc_IVH-5). Glc_IVH-5 also showed a COSY correlation to Glc_IVH-6 protons (δ_H3.55 and 3.78). Assignment of the ¹³C chemical shifts for Glc_IVC-2 (δ_C76.1), C-3 (δ_C78.8), C-4 (δ_C72.5), C-5 (δ_C81.7), and C-6 (δ_C65.8) was determined using the HSQC-DEPT data. HMBC correlations from Glc_IVH-3 to C-4 and C-5 and also from Glc_IVH-4 to C-3 and C-6 confirmed the assignments made above to complete the assignment of Glc_IV.
A summary of the ¹H and ¹³C chemical shifts for the glycoside at C-13 are found in the following table:


Position	¹³C^#	¹H

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 H₂SO₄and 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.