WO2014193888A1 - High-purity steviol glycosides - Google Patents
High-purity steviol glycosides Download PDFInfo
- Publication number
- WO2014193888A1 WO2014193888A1 PCT/US2014/039666 US2014039666W WO2014193888A1 WO 2014193888 A1 WO2014193888 A1 WO 2014193888A1 US 2014039666 W US2014039666 W US 2014039666W WO 2014193888 A1 WO2014193888 A1 WO 2014193888A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- reb
- rebaudioside
- composition
- steviol glycoside
- target steviol
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
- C07H1/00—Processes for the preparation of sugar derivatives
- C07H1/06—Separation; Purification
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P19/00—Preparation of compounds containing saccharide radicals
- C12P19/44—Preparation of O-glycosides, e.g. glucosides
- C12P19/56—Preparation of O-glycosides, e.g. glucosides having an oxygen atom of the saccharide radical directly bound to a condensed ring system having three or more carbocyclic rings, e.g. daunomycin, adriamycin
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Preparation or treatment thereof
- A23L2/52—Adding ingredients
- A23L2/60—Sweeteners
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
- A23L27/30—Artificial sweetening agents
- A23L27/33—Artificial sweetening agents containing sugars or derivatives
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
- A24B15/10—Chemical features of tobacco products or tobacco substitutes
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
- A24B15/18—Treatment of tobacco products or tobacco substitutes
- A24B15/28—Treatment of tobacco products or tobacco substitutes by chemical substances
- A24B15/30—Treatment of tobacco products or tobacco substitutes by chemical substances by organic substances
- A24B15/302—Treatment of tobacco products or tobacco substitutes by chemical substances by organic substances by natural substances obtained from animals or plants
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
- C07H15/00—Compounds containing hydrocarbon or substituted hydrocarbon radicals directly attached to hetero atoms of saccharide radicals
- C07H15/20—Carbocyclic rings
- C07H15/24—Condensed ring systems having three or more rings
- C07H15/256—Polyterpene radicals
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/10—Transferases (2.)
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/582—Recycling of unreacted starting or intermediate materials
Definitions
- 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.
- 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 CI 3 and CI 9. 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.
- compositions comprising steviol glycosides, including highly purified steviol glycoside compositions.
- the present invention provides a biocatalytic process for preparing a composition comprising a target steviol glycoside by contacting a starting composition comprising an organic substrate with a microorganism and/or biocatalyst, thereby producing a composition comprising a target steviol glycoside.
- the starting composition can be any organic compound comprising at least one carbon atom.
- the starting composition is selected from the group consisting of polyols or sugar alcohols, various carbohydrates.
- the target steviol glycoside can be any steviol glycoside.
- 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 , rebaudioside M2, rebaudioside D, rebaudioside D2, rebaudioside N, rebaudioside O or a synthetic steviol glycoside.
- the target steviol glycoside is stevioside.
- the target steviol glycoside is rebaudioside A.
- the target steviol glycoside is rebaudioside D.
- the target steviol glycoside is rebaudioside M (also known as rebaudioside X).
- the microorganism can be any microorganism possessing the necessary enzymes for converting the starting composition to target steviol glycosides.
- the biocatalysts will comprise at least one enzyme for converting the starting composition to target steviol glycosides.
- the biocatalysts can be located on the surface and/or inside the cell of the microorganism or can be secreted out of the microorganism.
- the biocatalyst can be whole cell suspension, crude lysate or purified enzymes.
- the biocatalyst can be in free form or immobilized to a solid support made from inorganic or organic materials.
- the enzymes necessary for converting the starting composition to target steviol glycosides include the steviol biosynthesis enzymes, UDP-glycosyltransferases (UGTs) and/or UDP-recycling enzyme.
- the steviol biosynthesis enzymes include mevalonate (MVA) pathway enzymes.
- the steviol biosynthesis enzymes include non-mevalonate 2-C-methyl-D-erythritol-4-phosphate pathway (MEP/DOXP) enzymes.
- the steviol biosynthesis enzymes are selected from the group including geranylgeranyl diphosphate synthase, copalyl diphosphate synthase, kaurene synthase, kaurene oxidase, kaurenoic acid 13-hydroxylase (KAH), steviol synthetase, deoxyxylulose 5 -phosphate synthase (DXS), D-l -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), l-hydroxy-2-methyl-2(E)- buteny
- 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.
- 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.
- the UDP-glucosyltransferases are synthesized.
- the UDP-glucosyltransferase is selected from group including UGT74G1, UGT85C2, UGT76G 1, UGT91D2 and UGTs having substantial (>85%) identity to these polypeptides as well as isolated nucleic acid molecules that code for these UGTs.
- steviol biosynthesis enzymes are present in one microorganism.
- the microorganism may be for example, E.coli, Saccharomyces sp., Aspergillus sp., Pichia sp,. Bacillus sp., Yarrowia sp.
- the UDP-glucosyltransferase is any UDP-glucosyltransferase capable of adding at least one glucose unit to rubusoside to form stevioside.
- the UDP-glucosyltransferase is UGT91D2.
- the UDP-glucosyltransferase is any UDP-glucosyltransferase capable of adding at least one glucose unit to stevioside to form rebaudioside A.
- the UDP-glucosyltransferase is UGT76G1.
- the UDP-glucosyltransferase is any UDP- glucosyltransferase capable of adding at least one glucose unit to rebaudioside A to form rebaudioside D.
- the UDP-glucosyltransferase is UGT91D2.
- the UGT is an improved variant of UGT91D2 with higher activity and/or selectivity produced by directed evolution.
- the UDP-glucosyltransferase is any UDP- glucosyltransferase capable of adding at least one glucose unit to rebaudioside D to form rebaudioside
- the UDP-glucosyltransferase is UGT76G1.
- the UGT is an improved variant of UGT76G1 with higher activity and/or selectivity produced by directed evolution.
- the method of the present invention further comprises recycling UDP to provide UDP-glucose.
- 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 (FIG. 3).
- the recycling catalyst is sucrose synthase.
- the recycling substrate is sucrose.
- the method of the present invention further comprises separating the target steviol glycoside from the starting 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.
- 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.
- 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.
- separation produces a composition comprising greater than about 90% by weight of the target steviol glycoside.
- the composition comprises greater than about 95% by weight of the target steviol glycoside.
- 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 novel steviol glycosides rebaudioside D2 (reb D2, isomer of rebaudioside D) and rebaudioside M2 (reb M2, isomer of rebaudioside M) , which are isomers of reb D and reb M, respectively.
- isolated and purified reb D2 is provided.
- isolated and purified reb M2 is provided.
- Reb D2 and reb M2 may also be present in any consumable products disclosed herein.
- 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.
- 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.
- 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.
- composition can be further purified to provide reb D2 or reb M2 with purities greater than about 95% by weight on a dry basis.
- FIG. 1 shows the structure of reb M.
- FIG. 2 shows the biocatalytic production of reb from stevioside.
- FIG. 3 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. 4 shows the IR spectrum of reb M.
- FIG. 5 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. 6. shows the HPLC chromatogram of purified reb M produced by biocatalysis from reb D.
- FIG. 7 shows the HPLC chromatogram of a reb M standard.
- FIG. 8 shows the HPLC chromatogram of co-injection of a reb M standard and reb M purified from biotransformation from reb D.
- FIG. 9 shows an overlay of the ⁇ NMR spectra of a reb M standard and reb M purified following biosynthesis from reb D.
- FIG. 10 shows the HRMS spectrum of reb M purified following biocatalytic production from reb D.
- FIG. 1 1 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. 12 shows the trace of semi-synthetic steviol glycoside mixture, Lot number CB- 2977-106. Chromatogram gridlines are not homogeneous as the detector was re-calibrated 14 min following injection.
- FIG. 13 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. 14 shows the ⁇ NMR spectrum of reb D2 (500 MHz, pyridine-d 5 ).
- FIG. 15 shows the 13 C NMR spectrum of reb 1)2(125 MHz, pyridine-d 5 ).
- FIG. 16 shows an expansion of the 13 C NMR spectrum of reb D2 (125 MHz, pyridine-d 5 ).
- FIG. 17 shows the ⁇ - ⁇ COSY Spectrum of reb D2 (500 MHz, pyridine-d 5 ).
- FIG. 18 shows the HSQC-DEPT spectrum of reb £>2(500 MHz, pyridine-d 5 ).
- FIG. 19 shows the HMBC spectrum of reb D2.
- FIG. 20 shows an expansion of HMBC spectrum of reb D2 (500 MHz, pyridine-ds).
- FIG. 21 shows the ⁇ NMR spectrum of reb 2(500 MHz, D 2 0).
- FIG. 22 shows the , 3 C NMR spectrum of reb M2 (125 MHz, D 2 0/TSP).
- FIG. 23 shows an expansion of the 13 C NMR spectrum of reb M2 (125 MHz, D 2 0/TSP).
- FIG. 24 shows the ⁇ - ⁇ COSY spectrum of reb M2 (500 MHz, D 2 0).
- FIG. 25 shows the HSQC-DEPT spectrum of reb 2(500 MHz, D 2 0).
- FIG. 26 shows the HMBC spectrum of reb M2 (500 MHz, D 2 0).
- FIG. 27 shows an expansion of HMBC spectrum of reb M2 (500 MHz, D 2 0).
- FIG. 28 shows another HMBC spectrum of reb M2.
- FIG. 29 shows a ⁇ NMR spectrum of reb M2.
- FIG. 30 shows a 13 C NMR spectrum of reb M2 .
- FIG. 31 shows another 13 C NMR spectrum of reb M2.
- FIG. 32 shows a ⁇ - ⁇ COSY spectrum of reb M2.
- FIG. 33 shows a HSQC-DEPT spectrum of reb M2.
- FIG. 34 shows an HMBC spectrum of reb M2.
- FIG. 35 shows another HMBC spectrum of reb M2.
- FIG. 36 shows a ID-TOCSY spectrum of reb M2.
- FIG. 37 shows a ID-TOCSY spectrum of reb M2.
- FIG. 38 shows a ID-TOCSY spectrum of reb M2.
- FIG. 39 shows a ID-TOCSY spectrum of reb M2.
- FIG. 40 shows an HPLC (CAD) analysis.
- FIG. 41 shows an HPLC (CAD) analysis.
- FIG. 42 shows an HPLC (CAD) analysis.
- FIG. 43 shows an HPLC (CAD) analysis.
- FIG. 44 shows an HPLC (CAD) analysis.
- FIG. 45 shows an HPLC (CAD) analysis.
- FIG. 46 shows an HPLC (CAD) analysis.
- FIG. 47 shows an HPLC (CAD) analysis.
- FIG. 48 shows an HPLC (CAD) analysis.
- FIG. 49 shows an HPLC (CAD) analysis.
- FIG. 50 shows an HPLC (CAD) analysis.
- FIG. 51 shows an HPLC (CAD) analysis.
- FIG. 52 shows an HPLC (CAD) analysis.
- FIG. 53 shows an LCMS chromatogram
- FIG. 54 shows an LCMS chromatogram
- FIG. 55 shows an LCMS chromatogram
- FIG. 56 shows an LCMS chromatogram.
- FIG. 57 shows a reaction profile.
- FIG. 58 shows an HPLC (CAD) analysis.
- FIG. 59 shows an HPLC (CAD) analysis.
- FIG. 60 shows an HPLC (CAD) analysis.
- FIG. 61 shows an HPLC (CAD) analysis.
- FIG. 62 shows an HPLC (CAD) analysis.
- FIG. 63 shows an LCMS chromatogram.
- FIG. 64 shows an HPLC (CAD) analysis.
- FIG. 65 shows an HPLC (CAD) analysis.
- FIG. 66 shows an HPLC (CAD) analysis.
- FIG. 67 shows an HPLC (CAD) analysis.
- FIG. 68 shows an HPLC (CAD) analysis.
- FIG. 69 shows the results of an HPLC analysis.
- the present invention provides a biocatalytic process for preparing a composition comprising a target steviol glycoside by contacting a starting composition, comprising an organic substrate, with a microorganism and/or biocatalyst, thereby producing a composition comprising a target steviol glycoside.
- biocatalysis or “biocatalytic” refers to the use of natural or genetically engineered biocatalysts, such as cells, protein enzymes, to perform single or multiple step chemical transformations on organic compounds.
- Biocatalysis include fermentation, biosynthesis and biotransformation processes. Both, isolated enzyme and whole-cell biocatalysis methods, using biocatalysts in free as well as immobilized forms, are known in the art.
- Biocatalyst protein enzymes can be naturally occurring or recombinant proteins.
- 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 /, rebaudioside E, rebaudioside H, rebaudioside L, rebaudioside K, rebaudioside J rebaudioside , rebaudioside M2, rebaudioside D, rebaudioside D2, rebaudioside N, rebaudioside O, synthetic steviol glycosides, e.g. enzymatically glucosylated steviol glycosides and combinations thereof.
- naturally occurring steviol glycosides e.g. steviolmonoside, steviol
- starting composition refers to any composition (generally an aqueous solution) containing one or more organic compound comprising at least one carbon atom.
- the starting composition is selected from the group consisting of polyols and various carbohydrates.
- 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.
- 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.
- 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.
- carbohydrate refers to aldehyde or ketone compounds substituted with multiple hydroxyl groups, of the general formula (CH 2 0) 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.
- carbohydrate derivatives substituted carbohydrate
- modified carbohydrates are synonymous.
- Modified carbohydrate means any carbohydrate wherein at least one atom has been added, removed, or substituted, or combinations thereof.
- 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, oxi
- the starting composition may be synthetic or purified (partially or entirely), commercially available or prepared.
- the starting composition is glycerol.
- the starting composition is glucose
- the starting composition is sucrose.
- the starting composition is starch.
- the starting composition is maltodextrin.
- the organic compound(s) of starting composition serve as a substrate(s) for the production of the target steviol glycoside(s), as described herein.
- the target steviol glycoside of the present method can be any steviol glycoside that can be prepared by the process disclosed herein.
- 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 /, 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.
- 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.
- the present invention is a biocatalytic process for the production of reb D.
- the present invention is a biocatalytic process for the production of reb D2.
- the present invention is a biocatalytic process for the production of reb M.
- the present invention is a biocatalytic process for the production of reb M2.
- the method of the present invention further comprises separating the target steviol glycoside from the starting 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.
- 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.
- 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.
- the process described herein 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.
- the process described herein 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.
- the process described herein when the target steviol glycoside is reb D, 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 99% reb D content by weight on a dry basis.
- the process described herein 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.
- the process described herein 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.
- the process described herein 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.
- the process described herein when the target steviol glycoside is reb I, the process described herein provides a composition comprising greater than about 90% reb / content by weight on a dry basis. In another particular embodiment, when the target steviol glycoside is reb /, the process described herein provides a composition comprising greater than about 95% reb / content by weight on a dry basis.
- the process described herein when the target steviol glycoside is stevioside, 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.
- a microorganism or biocatalyst is contacted with the starting composition to produce target steviol glycosides.
- the microorganism can be any microorganism possessing the necessary enzymes for converting the starting composition to target steviol glycosides. These enzymes are encoded within the microorganism's genome.
- the microoganism may be, for example, E.coli, Saccharomyces sp., Aspergillus sp., Pichia sp,. Bacillus sp., Yarrowia sp. etc.
- the enzymes can be located on the surface and/or inside the cell of the microorganism and/or can be secreted out in the medium by the microorganism.
- the biocatalyst comprises at least one enzyme and can be whole cell suspension, crude lysate or purified enzyme.
- the enzymes necessary for converting the starting composition to target steviol glycosides include the steviol biosynthesis enzymes and UDP-glycosyltransferases (UGTs).
- UDP-glycosyltransferases optionally it may include UDP recycling enzyme(s).
- the UDP recycling enzyme can be sucrose synthase and the recycling substrate can be sucrose.
- the steviol biosynthesis enzymes include mevalonate (MVA) pathway enzymes.
- the steviol biosynthesis enzymes include non-mevalonate 2-C-methyl-D-erythritol-4-phosphate pathway (MEP/DOXP) enzymes.
- the steviol biosynthesis enzymes are selected from the group including geranylgeranyl diphosphate synthase, copalyl diphosphate synthase, kaurene synthase, kaurene oxidase, kaurenoic acid 13-hydroxylase (KAH), steviol synthetase, deoxyxylulose 5 -phosphate synthase (DXS), D-l-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), l-hydroxy-2-methyl-2(E)- butenyl
- 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.
- the microorganism is free.
- the microorganism is immobilized.
- the microorganism may be immobilized to a solid support made from inorganic or organic materials.
- 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.
- the microorganism is in aqueous medium, comprising water, and various components selected form 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.
- the medium comprises buffer.
- Suitable buffers include, but are not limited to, PIPES buffer, acetate buffer and phosphate buffer.
- the medium comprises phosphate buffer.
- the medium can also include an organic solvent.
- 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.
- 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, UGTSL2.
- 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.
- 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.
- 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 or UGTSL2.
- the UDP-glucosyltransferase capable of adding at least one glucose unit to rebaudioside A is selected from the following listing of Genlnfo identifier numbers, preferably from the group presented in Table 1 , and more preferably the group presented in Table 2.
- 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.
- the method of the present invention further comprises recycling UDP to provide UDP-glucose.
- the method comprises 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. 3).
- a recycling catalyst i.e., a biocatalyst capable of UDP-glucose overproduction
- 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. 3).
- the UDP-glucose recycling catalyst is sucrose synthase.
- the recycling substrate is sucrose.
- the biocatalyst comprises more than one UDP- gl ucosy transferase .
- biocatalyst comprises more than one UDP-glucosyltransferase and UDP-glucose recycling catalyst.
- 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.
- Reb D2 is an isomer of reb D and has the following structure:
- 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.
- 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%o by weight or greater than about 99% by weight.
- the present invention also provides compositions comprising reb D2.
- the present invention 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.
- 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. 1 15454819 version NP_001051010.1 , GI No.
- the enzyme capable of transforming reb A to reb D2 can be immobilized or in a recombinant microorganism.
- the enzyme is immobilized. In another embodiment, the enzyme is in a recombinant microorganism.
- the microorganism is free.
- the microorganism is immobilized.
- the microorganism may be immobilized to a solid support made from inorganic or organic materials.
- 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., Yarrow ia sp.
- the microorganism is in an aqueous medium, comprising water, and various components selected form 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.
- 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.
- the enzyme is a UDP-glucosyltransferase capable of transforming reb A to reb D2.
- the enzyme is selected from UGT91D2, UGTSL, UGTSL_Sc, UGTSL2 (GI No. 460410132 version XP_004250485.1), GI No. 460409128 (UGTSL) verison XP_004249992.1, GI No. 1 15454819 version NP 001051010.1, GI No. 187373030, version ACD03249.1. GI No. 222619587 version EEE55719.1, GI No. 297795735 version XP_002865752.1 or EUGT1 1 and UGTs having substantial (>85%) sequence identity to these.
- the enzyme is UGTSL2 or its improved variant produced by directed evolution and having higher activity.
- 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.
- 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.
- isolation may result in a reb D2 purity less than about 95% by weight on an anhydrous basis
- 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.
- 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.
- HPLC is used to purify reb D2.
- semi-preparative HPLC is used to purify reb D2.
- a two-step semi-preparative HPLC purification can be used.
- the first step utilizes a C 18 column with a mobile phase containing A (25% MeCN in water) and B (30% MeCN in water) with the following gradient:
- the secondary step utilizes the same column and conditions, but with only an isocratic mobile phase: 20% MeCN in water.
- the present invention provides isolated and highly purified reb M2.
- Reb M2 is an isomer of reb and has the following structure:
- 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.
- 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.
- 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, in one embodiment, the present invention 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.
- 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.
- 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 XPJ)04250485.1), GI No. 460409128 (UGTSL) version XP 004249992.1, GI No. 1 15454819 version NP_001051010.1, GI No. 187373030, version ACD03249.1. GI No. 222619587 version EEE55719.1, GI No. 297795735 version XP_002865752.1 or EUGTl l .
- the enzyme can be immobilized or in a recombinant microorganism.
- the enzyme is immobilized. In another embodiment, the enzyme is in a recombinant microorganism.
- the microorganism is free.
- the microorganism is immobilized.
- the microorganism may be immobilized to a solid support made from inorganic or organic materials.
- 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.
- the microorganism is in aqueous medium, comprising water, and various components selected form 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.
- the medium comprises buffer.
- Suitable buffers include, but are not limited to, PIPES buffer, acetate buffer and phosphate buffer.
- the medium comprises phosphate buffer.
- the medium can also include an organic solvent.
- the enzyme is a UDP-glucosyltransferase capable of transforming reb A and/or reb D2 to reb M2 and is contained in E.coli.
- the enzyme is selected from UGT91D2, UGTSL, UGTSL_Sc, UGTSL2 (GI No. 460410132 version XP_004250485.1), GI No. 460409128 (UGTSL) verison XP 004249992.1, GI No. 1 15454819 version NP_001051010.1 , GI No. 187373030, version ACD03249.1. GI No. 222619587 version EEE55719.1, GI No. 297795735 version XP_002865752.1 or EUGTl l .
- the enzyme is UGTSL2 or its improved variant produced by directed evolution and having higher activity.
- the target steviol glycoside reb M2 can be produced within the microorganism.
- the target steviol glycoside can be secreted out in the medium.
- the released steviol glycoside can be continuously removed from the medium.
- the target steviol glycoside is separated 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.
- 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.
- 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.
- 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.
- HPLC is used to purify reb M2.
- semi-preparative HPLC is used to purify reb M2.
- a two-step semi-preparative HPLC purification can be used.
- the first step utilizes a CI 8 column with a mobile phase containing A (25% MeCN in water) and B (30% MeCN in water) with the following gradient:
- the secondary step utilizes the same column and conditions, but with only an isocratic mobile phase: 20% MeCN in water.
- Purified steviol glycosides 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 C 56 H 9 o0 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.
- the infrared absorption spectrum is shown in FIG. 4.
- 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 at least one sweetener, flavor, food ingredient and/or combination thereof.
- Non-limiting examples of flavors include lime, lemon, orange, fruit, banana, grape, pear, pineapple, mango, berry, bitter almond, cola, cinnamon, sugar, cotton candy and vanilla flavors and/or combination thereof.
- Non-limiting examples of other food ingredients include at least one selected from flavors, acidulants, organic and amino acids, coloring agents, bulking agents, modified starches, gums, texturizers, preservatives, antioxidants, emulsifiers, stabilizers, thickeners and gelling agents and/or combination 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/or combination 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 at least one naturally occurring high intensity sweeteners such as stevioside, reb A, reb B, reb C, reb D, reb E, reb F, steviolbioside, dulcoside A, rubusoside, mogrosides, brazzein, neohesperidin dihydrochalcone, glycyrrhizic acid and its salts, thaumatin, perillartine, pernandulcin, mukuroziosides, baiyunoside, phlomisoside- I, dimethyl-hexahydrofluorene-dicarboxylic acid, abrusosides, periandrin, carnosiflosides, cyclocarioside, pte
- 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, erythritol and/or 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 the like.
- synthetic high intensity sweeteners such as sucralose, potassium acesulfame, aspartame, alitame, saccharin, neohesperidin dihydrochalcone, cyclamate, neotame, dulcin, suosan advantame, salts thereof, and the like.
- 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 and tryptophan.
- 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.
- 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, flavor
- 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.
- 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.
- 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.
- 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 D-tagatose, allulose, allose, L-sugars, L-sorbose, L-arabinose, and others.
- Highly purified target steviol glycoside(s), particularly, reb D, reb D2, reb M and/or reb M2 may also be combined with various carbohydrates.
- Carbohydrate generally refers to aldehyde or ketone compounds substituted with multiple hydroxyl groups, of the general formula (CH 2 0) 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.
- 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
- 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.
- 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
- 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.
- a tabletop sweetener comprising reb D2 is provided.
- 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.
- the present invention is also directed to sweetness enhancement in beverages using reb M2.
- 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.
- sweetness enhancer refers to a compound capable of enhancing or intensifying the perception of sweet taste in a composition, such as a beverage.
- sweetness enhancer is synonymous with the terms “sweet taste potentiator,” “sweetness potentiator,” “sweetness amplifier,” and “sweetness intensifier.”
- sweetness recognition threshold concentration 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).
- 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.
- 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 1 1.0% by weight, about 1 1.5% by weight or about 12.0% by weight.
- 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.
- 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.
- the sweetener is erythritol.
- 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.
- a sweetener can be used alone, or in combination with other sweeteners.
- the rare sugar is D-allose.
- 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%.
- the rare sugar is D-psicose.
- 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%.
- the rare sugar is D-ribose.
- 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%.
- the rare sugar is D-tagatose.
- 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%.
- the rare sugar is L-glucose.
- 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%.
- the rare sugar is L-fucose.
- 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%.
- the rare sugar is L-arabinose.
- 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%.
- the rare sugar is D-turanose.
- 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%.
- the rare sugar is D-leucrose.
- 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.
- 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.
- 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 UGT76Gl_pET30a+ plasmid was introduced in E. coli B121(DE3) and E. coli EC 100 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 aliquots were stored at -20 °C and at -80 °C.
- E. coli BL21(DE3) containing the pET30A+_UGT76Gl 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.
- the S30 T7 High Yield Protein expression system kit from Promega was used. 4 ⁇ g of UGT76Gl_pET30a+ plasmid from E. coli ECI OO was mixed with 80 ⁇ of S30 premix plus and 72 of S30 T7 extract was added. Nuclease-free water was added in order to obtain a total volume of 200 ⁇ , and the resulting solution was incubated for 2 h at 30°C. 180 ⁇ L ⁇ was used in the catalytic test reaction.
- the UGT91D2_pET30a+ plasmid was introduced into E. coli ECIOO 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 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.
- the total volume of the reaction was 5.0 mL with the following composition: 50 mM sodium phosphate buffer pH 7.2, 3 mM MgCl 2 , 2.5 mM UDP-glucose, 0.5 mM Stevioside and 500 ⁇ ⁇ of UGT76G1 thawed lysate.
- the reactions were run at 30 °C on an orbitary shaker at 135 rpm.
- 460 ⁇ of the reaction mixture was quenched with 40 ⁇ , of 2N H 2 S0 4 and 420 ⁇ , 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 as seen in Figure 40.
- UGT76G1 catalyzed transformation of stevioside to Reb A
- the total volume of the reaction was 0.5 mL with the following composition: 50 mM sodium phosphate buffer pH 7.2, 3 mM MgCl 2 , 3.8 mM UDP-glucose, 0.1 mM Rebaudioside A and 180 of in-vitro produced UGT91D2.
- the reactions were run at 30 °C on an orbitary shaker at 135 rpm.
- 450 of reaction mixture was quenched with 45 ⁇ of 2N H 2 S0 4 and 405 ⁇ , 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.
- the total volume of the reaction was 2 mL with the following composition: 50 mM sodium phosphate buffer pH 7.2, 3 mM MgCl 2 , 3.8 mM UDP-glucose, 0.5 mM Rebaudioside D and 180 ⁇ ⁇ of in-vitro produced UGT76G1.
- the reactions were run at 30 °C on an orbitary shaker at 135 rpm.
- 400 ⁇ , of reaction mixture was quenched with 40 ⁇ , of 2N H 2 S0 4 and 360 ⁇ , 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 as seen in Figure 41.
- 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)
- the pET30a+_UGT76Gl 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 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.
- the pET30a+_UGT76Gl plasmid was transformed into Tuner (DE3) expression strain (Novagen Tuner tm (DE3) Competent cells) by heat shock treatment.
- Tuner (DE3) expression strain (Novagen Tuner tm (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 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 ⁇ . 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.
- the pMAL_UGT76Gl 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 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.
- the pMAL_UGT76Gl plasmid was transformed into ArticExpress expression strain (Agilent ArcticExpress competent cells) by heat shock treatment.
- ArticExpress expression strain 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 aliquots were stored at -20°C and at -80°C.
- 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.
- the pCOLDIII_UGT76Gl 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 aliquots were stored at -20°C and at -80°C.
- 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.
- the pCOLDIII_UGT76Gl plasmid was transformed into Origami2 (DE3) expression strain (Novagen OrigamiTM2 (DE3) Competent Cells) by heat shock treatment.
- Origami2 (DE3) expression strain Novagen OrigamiTM2 (DE3) Competent Cells
- 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 ⁇ aliquots were stored at - 20°C and at -80°C.
- Example 12 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 MgCl 2 , 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).
- HPLC trace of the product mixture is shown in FIG. 5.
- 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 ⁇ / ⁇ .
- the column used was Phenomenex Prodigy 5 ⁇ ODS (3) 100 A; 250x2mm. The column temperature was maintained at 40 °C. The injection volume was 20-40 ⁇ .
- the pMAL_UGT91 D2 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 ⁇ 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 12.32g.
- 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 ⁇ ⁇ aliquots were stored at -20°C and at -80°C.
- 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.
- the pET30a+_UGT91D2 plasmid was transformed into Tuner (DE3) expression strain (Novagen Tuner tm (DE3) Competent cells) by heat shock treatment.
- Tuner (DE3) expression strain (Novagen Tuner tm (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 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 of a 100 mM IPTG solution was added (IPTG concentration in medium is 100 ⁇ ) 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.
- 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 ⁇ , aliquots were stored at -20°C and at -80°C.
- 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 16h. 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.
- aminoacid sequences are as follows: SEQ ID 3
- the tested plasmids were received in a microtiterplate containing a plasmid as freeze-dried solid in each separate well.
- Transformation of competent cells with plasmids Aliquots of chemically competent EC 100 cells were taken from freezer at -80°C and stored on ice. The cells were allowed to thaw on ice for 10 minutes. 10 ⁇ 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 ⁇ 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.
- the remainder of the culture was centrifuged at 5,525g 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:
- HPLC assay was performed as follows:
- HPLC assay results are provided below:
- the enzyme SI 15N05 A 7 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, as seen in Figures 42- 46.
- EUGT1 1 gene as was described in the Patent application WO/2013/022989A2 was synthesized by DNA2.0 and subsequently subcloned in pET30a+ vector.
- amino-acid sequence is as follows: SEQ ID 8
- the tested plasmid was received in a microtiterplate containing a plasmid as freeze-dried solid in a separate well.
- Plasmid quantity was determined as follows:
- Transformation of competent cells with plasmid An aliquot of chemically competent EC 100 cells was taken from freezer at -80 °C and stored on ice. The cells were allowed to thaw on ice for 10 minutes. 10 ⁇ 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 ⁇ , 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.
- 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:
- 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 ⁇ , of the mixture was frozen whereas the remainder was used for the catalytic test for the conversion of Rebaudioside A to Rebaudioside D.
- HPLC Analysis The HPLC assay was performed as described in EXAMPLE 20.
- HPLC assay results are provided below:
- 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 iL aliquots were stored at -20°C and at -80°C.
- 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).
- 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 8hrs.
- 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 40hrs, the cells were harvested by centrifugation and frozen. The following yields of cell wet weights (CWW) are mentioned below.
- Lysis was performed by addition of Bugbuster Master mix (Novagen) and the lysate was recovered by centrifugation and used fresh.
- HPLC Analysis The HPLC assay was performed as described in EXAMPLE 20.
- reaction mixtures representing GI No. 460409128 particularly the sample "12400 S1 15N05A7 T24h 130627ABA" of EXAMPLE 20 (hereinafter S1 15N05A7), and the sample “12400 S129N04 T45h 130712ABA” of 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 61 10A MSD, and interfaced with "LC/MSD Chemstation” software, was used.
- reaction mixture representing GI No. 460409128 particularly the sample "12400 S 129N04 T45h 130712ABA" of EXAMPLE 22 (hereinafter S129N04) were additionally assayed by LC-MS, as seen in Figures 55-56, along with Stevia rebaudiana Bertoni leaf extract "MLDl” produced by PureCircle Sdn Bhd (Malaysia) to determine the occurrence of S 129N04 glycosides in nature.
- the assay shows that the compound observed on LCMS system at 3.5min, in EXAMPLE 23 (C56H 90 O33; later confirmed as reb Ml), and the compound observed on LCMS system at 7.6min, in EXAMPLE 23 (C 5 oH 8 o0 2 8 ; reb UNK; later confirmed as reb D2) occur in the extract of Stevia rebaudiana Bertoni plant.
- E. coli BL21(DE3) containing the pET30a+_UGT76Gl var 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.
- 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 of fresh lysate that was added to a solution of ebaudioside D (final concentration 0.5 mM), MgCl 2 (final concentration 3 mM) and UDP-Glucose (final concentration 2.5 mM) in 50 mM phosphate buffer pH 7.2.
- UGTSL2 (GI_460410132 / XP_004250485.1) amino acid sequence:
- 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 aliquots were stored at -20°C and at -80°C.
- 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.
- 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.
- UGTSL was prepared according to EXAMPLE 22, and UGTSL2 was prepared according to EXAMPLE 27.
- UGTSL was prepared according to EXAMPLE 22, and UGTSL2 was prepared according to EXAMPLE 27.
- UGTSL2 was prepared according to EXAMPLE 27.
- reaction mixtures prepared according to EXAMPLE 30 and incubated for 45hrs was analyzed by LC-MS, along with Sterna rebaudiana Bertoni leaf extract "MLD1" produced by PureCircle Sdn Bhd (Malaysia), to determine the occurrence of formed glycosides in nature.
- the assay shows that the compound observed on LC-MS system at 1 1.77min is the same as the compound at 3.5min, in EXAMPLE 23 (C56H 0O33; later confirmed as reb M2), and the compound observed at 26.64 min is the same as the compound at 7.6min, in EXAMPLE 23 (C 5 oH 8 o0 2 8; reb UNK; later confirmed as reb D2).
- Other isomers of reb M were observed at 13.96min and also another isomer form of reb D was observed at 25.06min. All observed compounds occurred in the extract of Stevia rebaudiana Bertoni plant.
- 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 iL aliquots were stored at -20°C and at -80°C.
- 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.
- reaction mixtures were analyzed by LCMS to determine all reaction products.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Zoology (AREA)
- Wood Science & Technology (AREA)
- Genetics & Genomics (AREA)
- Biotechnology (AREA)
- Biochemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Nutrition Science (AREA)
- Polymers & Plastics (AREA)
- Food Science & Technology (AREA)
- Microbiology (AREA)
- General Engineering & Computer Science (AREA)
- Molecular Biology (AREA)
- Botany (AREA)
- Agronomy & Crop Science (AREA)
- Toxicology (AREA)
- Proteomics, Peptides & Aminoacids (AREA)
- Medicinal Chemistry (AREA)
- Biomedical Technology (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Seasonings (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Saccharide Compounds (AREA)
Abstract
Description
Claims
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| MX2019005688A MX395693B (en) | 2013-05-28 | 2014-05-28 | HIGH PURITY STEVIOL GLYCOSIDES. |
| EP14804243.5A EP3004127A4 (en) | 2013-05-28 | 2014-05-28 | High-purity steviol glycosides |
| MX2015016362A MX365044B (en) | 2013-05-28 | 2014-05-28 | High-purity steviol glycosides. |
| CN201480036885.9A CN105408339B (en) | 2013-05-28 | 2014-05-28 | High-purity steviol glycosides |
| BR112015030082A BR112015030082A2 (en) | 2013-05-28 | 2014-05-28 | high purity steviol glycosides |
Applications Claiming Priority (22)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201361827922P | 2013-05-28 | 2013-05-28 | |
| US61/827,922 | 2013-05-28 | ||
| US201361843544P | 2013-07-08 | 2013-07-08 | |
| US61/843,544 | 2013-07-08 | ||
| US201361861528P | 2013-08-02 | 2013-08-02 | |
| US61/861,528 | 2013-08-02 | ||
| US201361881166P | 2013-09-23 | 2013-09-23 | |
| US61/881,166 | 2013-09-23 | ||
| US201361885084P | 2013-10-01 | 2013-10-01 | |
| US61/885,084 | 2013-10-01 | ||
| US201361904751P | 2013-11-15 | 2013-11-15 | |
| US61/904,751 | 2013-11-15 | ||
| US201361913482P | 2013-12-09 | 2013-12-09 | |
| US61/913,482 | 2013-12-09 | ||
| US201361921635P | 2013-12-30 | 2013-12-30 | |
| US61/921,635 | 2013-12-30 | ||
| US201461925329P | 2014-01-09 | 2014-01-09 | |
| US61/925,329 | 2014-01-09 | ||
| US201461939855P | 2014-02-14 | 2014-02-14 | |
| US61/939,855 | 2014-02-14 | ||
| US14/287,837 US9752174B2 (en) | 2013-05-28 | 2014-05-27 | High-purity steviol glycosides |
| US14/287,837 | 2014-05-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2014193888A1 true WO2014193888A1 (en) | 2014-12-04 |
Family
ID=51985807
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2014/039758 Ceased WO2014193934A1 (en) | 2013-05-28 | 2014-05-28 | High-purity steviol glycosides |
| PCT/US2014/039666 Ceased WO2014193888A1 (en) | 2013-05-28 | 2014-05-28 | High-purity steviol glycosides |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2014/039758 Ceased WO2014193934A1 (en) | 2013-05-28 | 2014-05-28 | High-purity steviol glycosides |
Country Status (7)
| Country | Link |
|---|---|
| US (5) | US9752174B2 (en) |
| EP (2) | EP3004128A4 (en) |
| CN (4) | CN112538512A (en) |
| BR (2) | BR112015030082A2 (en) |
| CA (2) | CA2913252C (en) |
| MX (4) | MX365044B (en) |
| WO (2) | WO2014193934A1 (en) |
Cited By (28)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2793618A1 (en) | 2011-12-19 | 2014-10-29 | The Coca-Cola Company | Methods for purifying steviol glycosides and uses of the same |
| WO2016196345A1 (en) | 2015-05-29 | 2016-12-08 | Cargill, Incorporated | Heat treatment to produce glycosides |
| WO2016196368A1 (en) | 2015-05-29 | 2016-12-08 | Cargill, Incorporated | Fermentation methods for producing steviol glycosides with multi-phase feeding |
| WO2016196321A1 (en) | 2015-05-29 | 2016-12-08 | Cargill, Incorporated | Fermentation methods for producing steviol glycosides using high ph and compositions obtained therefrom |
| US9771434B2 (en) | 2011-06-23 | 2017-09-26 | Purecircle Sdn Bhd | Products from stevia rebaudiana |
| WO2018031955A2 (en) | 2016-08-12 | 2018-02-15 | Amyris, Inc. | Udp-dependent glycosyltransferase for high efficiency production of rebaudiosides |
| WO2019033064A1 (en) | 2017-08-11 | 2019-02-14 | Amyris, Inc. | Pisum sativum kaurene oxidase for high efficiency production of rebaudiosides |
| JP2019536444A (en) * | 2016-10-21 | 2019-12-19 | ペプシコ・インク | Method for preparing rebaudioside J using an enzymatic method |
| US10602762B2 (en) | 2011-02-17 | 2020-03-31 | Purecircle Sdn Bhd | Glucosylated steviol glycoside as a flavor modifier |
| WO2020081468A1 (en) | 2018-10-15 | 2020-04-23 | Amyris, Inc. | Stevia rebaudiana kaurenoic acid hydroxylase variants for high efficiency production of rebaudiosides |
| US10696706B2 (en) | 2010-03-12 | 2020-06-30 | Purecircle Usa Inc. | Methods of preparing steviol glycosides and uses of the same |
| US10711024B2 (en) | 2014-12-17 | 2020-07-14 | Cargill, Incorporated | Steviol glycoside compounds, compositions for oral ingestion or use, and method for enhancing steviol glycoside solubility |
| WO2020154549A2 (en) | 2019-01-24 | 2020-07-30 | Amyris, Inc. | Abc transporters for the high efficiency production of rebaudiosides |
| US10780170B2 (en) | 2013-06-07 | 2020-09-22 | Purecircle Sdn Bhd | Stevia extract containing selected steviol glycosides as flavor, salty and sweetness profile modifier |
| US10815514B2 (en) | 2016-05-16 | 2020-10-27 | Evolva Sa | Production of steviol glycosides in recombinant hosts |
| US10844414B2 (en) | 2015-08-06 | 2020-11-24 | Cargill, Incorporated | Methods for producing steviol glycosides in engineered yeast |
| US10952458B2 (en) | 2013-06-07 | 2021-03-23 | Purecircle Usa Inc | Stevia extract containing selected steviol glycosides as flavor, salty and sweetness profile modifier |
| JP2021087439A (en) * | 2021-02-18 | 2021-06-10 | ペプシコ・インク | Method for preparing rebaudioside j using enzymatic method |
| US11202461B2 (en) | 2014-09-02 | 2021-12-21 | Purecircle Sdn Bhd | Stevia extracts |
| JP2022501309A (en) * | 2018-09-29 | 2022-01-06 | フイルメニツヒ ソシエテ アノニムFirmenich Sa | Terpene glycoside derivatives and their use |
| US11344051B2 (en) | 2015-04-03 | 2022-05-31 | Dsm Ip Assets B.V. | Steviol glycosides |
| WO2022187819A1 (en) | 2021-03-01 | 2022-09-09 | Cargill, Incorporated | Xylosylated steviol glycosides and enzymatic methods for production |
| US11647771B2 (en) | 2015-10-26 | 2023-05-16 | Purecircle Usa Inc. | Steviol glycoside compositions |
| US11653686B2 (en) | 2015-12-15 | 2023-05-23 | Purecircle Usa Inc. | Steviol glycoside compositions |
| US11690391B2 (en) | 2011-02-17 | 2023-07-04 | Purecircle Sdn Bhd | Glucosylated steviol glycoside as a flavor modifier |
| US12065685B1 (en) | 2019-05-13 | 2024-08-20 | Amyris, Inc. | UDP-glycosyltransferase variants and uses thereof |
| WO2024228615A1 (en) | 2023-05-03 | 2024-11-07 | Purecircle Sdn. Bhd. | High-purity steviol glycosides |
| US12479877B2 (en) | 2010-03-12 | 2025-11-25 | The Coca-Cola Company | Methods for purifying steviol glycosides and uses of the same |
Families Citing this family (88)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2826861B1 (en) | 2012-03-16 | 2020-04-29 | Suntory Holdings Limited | Steviol glycosyltransferase and gene encoding same |
| US10113154B2 (en) | 2012-03-27 | 2018-10-30 | Suntory Holdings Limited | Method for producing steviol glycoside |
| US9752174B2 (en) | 2013-05-28 | 2017-09-05 | Purecircle Sdn Bhd | High-purity steviol glycosides |
| MX395285B (en) | 2012-05-22 | 2025-03-25 | Purecircle Sdn Bhd | HIGH PURITY STEVIOL GLUCOSIDES. |
| TW201402599A (en) | 2012-05-30 | 2014-01-16 | Suntory Holdings Ltd | Steviol glycosyltransferase and gene coding the same |
| CN103397064B (en) | 2013-08-14 | 2015-04-15 | 苏州汉酶生物技术有限公司 | Method for preparing rebaudioside M through enzyme method |
| US9522929B2 (en) | 2014-05-05 | 2016-12-20 | Conagen Inc. | Non-caloric sweetener |
| EP3683315A1 (en) * | 2014-08-19 | 2020-07-22 | Purecircle SDN BHD | Method for preparing rebaudioside m |
| MX389746B (en) * | 2014-09-19 | 2025-03-20 | Purecircle Sdn Bhd | High-purity steviol glycosides |
| WO2016052659A1 (en) | 2014-09-30 | 2016-04-07 | サントリー食品インターナショナル株式会社 | Carbonated beverage, syrup to be used for preparing carbonated beverage, method for manufacturing carbonated beverage, and method for suppressing generation of bubbles in carbonated beverage |
| MX368414B (en) | 2014-10-03 | 2019-10-02 | Conagen Inc | Non-caloric sweeteners and methods for synthesizing. |
| WO2016073740A1 (en) * | 2014-11-05 | 2016-05-12 | Manus Biosynthesis, Inc. | Microbial production of steviol glycosides |
| US10604743B2 (en) | 2015-03-16 | 2020-03-31 | Dsm Ip Assets B.V. | UDP-glycosyltransferases |
| EP3274448B1 (en) * | 2015-03-23 | 2021-08-11 | DSM IP Assets B.V. | Udp-glycosyltransferases from solanum lycopersicum |
| AU2016250184B2 (en) | 2015-04-14 | 2020-07-30 | Conagen Inc. | Production of non-caloric sweeteners using engineered whole-cell catalysts |
| CA2991662A1 (en) * | 2015-07-10 | 2017-01-19 | Dsm Ip Assets B.V. | Steviol glycoside composition |
| US20190203244A1 (en) * | 2015-08-20 | 2019-07-04 | Pepsico, Inc. | Preparation of rebaudioside m in a single reaction vessel |
| RU2727426C2 (en) * | 2015-08-27 | 2020-07-21 | Пьюрсёркл Сдн Бхд | Stevia extracts |
| JP6109353B1 (en) | 2016-01-05 | 2017-04-05 | サントリー食品インターナショナル株式会社 | Beverage, method for producing beverage, and method for suppressing foaming of beverage |
| CN108777992A (en) * | 2016-01-07 | 2018-11-09 | 谱赛科美国股份有限公司 | Highly dissoluble steviol glycoside |
| AU2017241865B2 (en) * | 2016-03-31 | 2019-10-03 | Suntory Holdings Limited | Stevia-containing beverage |
| NZ747256A (en) | 2016-03-31 | 2020-04-24 | Suntory Holdings Ltd | Beverage containing tea polymerized polyphenol and rebd and/or rebm |
| WO2017189994A1 (en) * | 2016-04-29 | 2017-11-02 | Pepsico, Inc. | Novel steviol glycosides blends |
| CN105919016A (en) * | 2016-04-29 | 2016-09-07 | 清流县冠裕食品有限公司 | Formula for sweetening agent used for canned food |
| WO2017196933A1 (en) * | 2016-05-10 | 2017-11-16 | The Coca-Cola Company | Methods of freeze drying compositions containing rebaudioside m and rebaudioside d |
| WO2017218325A1 (en) | 2016-06-15 | 2017-12-21 | Codexis, Inc. | Engineered beta-glucosidases and glucosylation methods |
| US10494397B2 (en) * | 2016-07-15 | 2019-12-03 | Pepsico, Inc. | Rebaudioside analogs |
| CA3032656A1 (en) | 2016-08-09 | 2018-02-15 | Dsm Ip Assets B.V. | Crystallization of steviol glycosides |
| US10085472B2 (en) | 2016-08-29 | 2018-10-02 | Pepsico, Inc. | Compositions comprising rebaudioside J |
| JP2019528761A (en) * | 2016-10-07 | 2019-10-17 | シージェイ チェイルジェダン コーポレーションCj Cheiljedang Corporation | Method for improving alcohol feeling of alcoholic beverages using allulose |
| RU2019114181A (en) * | 2016-10-14 | 2020-11-16 | Конаджен Инк. | BIOSYNTHETIC OBTAINING OF STEVIOL GLYCOSIDES AND RELATED METHODS |
| CN109890973B (en) * | 2016-10-21 | 2023-05-23 | 百事可乐公司 | A method for enzymatically preparing rebaudioside N |
| EP3530746A4 (en) * | 2016-10-21 | 2020-06-24 | Pepsico, Inc. | Method for preparing rebaudioside c using enzymatic method |
| WO2019099118A1 (en) * | 2017-11-14 | 2019-05-23 | Purecircle Usa Inc. | Stevia-derived molecules, methods of obtaining such molecules, and uses of the same |
| WO2018090020A1 (en) | 2016-11-14 | 2018-05-17 | Purecircle Usa Inc. | Stevia-derived molecules, methods of obtaining such molecules, and uses of the same |
| CN110475482A (en) * | 2016-11-16 | 2019-11-19 | 可口可乐公司 | Taste Improvement in Stevia-Sweetened Beverages Using Miracle Fruit |
| CN106834389B (en) * | 2016-12-13 | 2020-03-17 | 南京工业大学 | Method for preparing rebaudioside M2 by catalyzing rebaudioside A through recombinant bacteria |
| CN106754595B (en) * | 2016-12-13 | 2019-10-22 | 南京工业大学 | A Recombinant Bacteria and Its Application in Catalyzing Rebaudioside A to Rebaudioside D |
| WO2018112189A1 (en) * | 2016-12-14 | 2018-06-21 | The Coca-Cola Company | Preparing novel steviol glycosides by bioconversion |
| AU2018215335B2 (en) | 2017-02-03 | 2020-10-01 | Tate & Lyle Solutions Usa Llc | Engineered glycosyltransferases and steviol glycoside glucosylation methods |
| CN108441369A (en) * | 2017-02-16 | 2018-08-24 | 新疆唐庭霞露酒庄有限公司 | A kind of preparation method of ice-wine |
| MX389414B (en) | 2017-02-24 | 2025-03-20 | Corn Products Dev Inc | USE OF STEVIOL GLYCOSIDE IN MALTING. |
| WO2018165330A1 (en) * | 2017-03-08 | 2018-09-13 | Purecircle Usa Inc. | High rebaudioside m stevia plant cultivars and methods of producing the same |
| PE20200291A1 (en) * | 2017-05-15 | 2020-02-05 | Purecircle Usa Inc | HIGH PURITY STEVIOL GLYCOSIDES |
| WO2018213290A1 (en) * | 2017-05-15 | 2018-11-22 | Purecircle Usa Inc. | High-purity steviol glycosides |
| MX2019015404A (en) | 2017-06-30 | 2020-07-20 | Conagen Inc | Hydrolysis of steviol glycosides by beta-glucosidase. |
| US11432573B2 (en) * | 2017-07-27 | 2022-09-06 | Franco Cavaleri | Food and beverage sweeteners |
| CN109423486B (en) * | 2017-08-29 | 2022-02-25 | 中国科学院分子植物科学卓越创新中心 | Novel UDP-glycosyltransferase and its application |
| US11365417B2 (en) | 2017-09-12 | 2022-06-21 | Bio Capital Holdings, LLC | Biological devices and methods of use thereof to produce steviol glycosides |
| WO2019090336A1 (en) * | 2017-11-06 | 2019-05-09 | Purecircle Usa Inc. | High-purity steviol-glycosides |
| EP3765627A4 (en) * | 2018-03-12 | 2021-10-13 | Conagen Inc. | BIOSYNTHETIC PRODUCTION OF STEVIOL GLYCOSIDES REBAUDIOSIDE J AND REBAUDIOSIDE N |
| JP7402168B2 (en) * | 2018-03-14 | 2023-12-20 | ザ コカ・コーラ カンパニー | Concentrates and uses containing stevia blends |
| AU2018413277B2 (en) * | 2018-03-16 | 2024-07-11 | Purecircle Usa Inc. | High-purity steviol glycosides |
| WO2019178471A1 (en) * | 2018-03-16 | 2019-09-19 | Purecircle Usa Inc. | High-purity steviol glycosides |
| MX2020009635A (en) * | 2018-03-16 | 2021-02-16 | Purecircle Usa Inc | High-purity steviol glycosides. |
| CA3100539A1 (en) | 2018-05-17 | 2019-11-21 | The Coca-Cola Company | Process for preparing concentrated solutions of steviol glycosides, and uses |
| CN108753748B (en) * | 2018-06-08 | 2021-12-10 | 中国中医科学院中药研究所 | Emodin glycosyltransferase protein FtUGT75R2, and coding gene and application thereof |
| CN112638176A (en) * | 2018-06-28 | 2021-04-09 | 株式会社三养社 | Mixed sugar compositions comprising malto-oligosaccharides |
| BR112021001661A8 (en) | 2018-07-30 | 2022-08-09 | Codexis Inc | Modified glyclytransferase, modified polynucleotide, vector, host cell, methods to produce at least one modified glyclytransferase, to produce at least one variant of sucrose synthase, to glycosillation of a substrate, to produce refudiosido, refudiosidade A and/or regaudiosido I, and regradiosido D, COMPOSITION, MODIFIED SUCROSE SYNTHASE, AT LEAST ONE REBAUDIOSIDE, REBAUDIOSIDE M, REBAUDIOSIDE A, REBAUDIOSIDE I, E, REBAUDIOSIDE D. |
| JP7498708B2 (en) | 2018-11-09 | 2024-06-12 | ギンゴー バイオワークス, インコーポレイテッド | Mogroside biosynthesis |
| CN109750072B (en) * | 2019-01-31 | 2022-04-19 | 南京工业大学 | A kind of method for preparing rebaudioside E by enzymatic method |
| CN109750071A (en) * | 2019-01-31 | 2019-05-14 | 南京工业大学 | Method for synthesizing rebaudioside M through biocatalysis |
| CA3130257A1 (en) * | 2019-02-15 | 2020-08-20 | Purecircle Usa Inc. | High-purity steviol glycosides |
| MX2021011908A (en) * | 2019-04-01 | 2021-12-15 | Coca Cola Co | COMPOSITIONS CONTAINING BRAZEINE. |
| WO2020237226A1 (en) * | 2019-05-23 | 2020-11-26 | Arzeda Corp. | Compositions and methods for producing steviol glycosides |
| CN112080480B (en) * | 2019-06-14 | 2023-01-03 | 中国科学院分子植物科学卓越创新中心 | Glycosyltransferase mutants and uses thereof |
| CN110669809B (en) * | 2019-11-12 | 2022-12-23 | 广西师范大学 | Method for preparing mogroside IV and mogroside V by enzyme method |
| EP4040986B1 (en) * | 2019-12-13 | 2025-12-24 | Firmenich Incorporated | Taste modifying compositions and uses thereof |
| CN111187316B (en) * | 2020-02-14 | 2021-06-15 | 南京全凯生物基材料研究院有限公司 | Method for extracting rebaudioside D and rebaudioside M from stevioside mother liquor |
| CN115768281A (en) * | 2020-04-20 | 2023-03-07 | 嘉吉公司 | Steviol glycoside malonate |
| US20230172235A1 (en) * | 2020-05-07 | 2023-06-08 | The Coca-Cola Company | Beverages comprising rebaudioside am and rebaudioside m with enhanced flavor |
| CN112760302B (en) * | 2020-12-23 | 2022-08-26 | 中化健康产业发展有限公司 | Glycosyltransferase StUGT capable of catalyzing rebaudioside A to generate rebaudioside D |
| JP2022103561A (en) * | 2020-12-28 | 2022-07-08 | サントリーホールディングス株式会社 | Beverages containing D-arabinose |
| BR112023016512A2 (en) * | 2021-02-17 | 2023-10-24 | Arzeda Corp | COMPOSITIONS AND METHODS FOR PRODUCING REBAUDIOSIDE D |
| JP2024516296A (en) * | 2021-05-04 | 2024-04-12 | ザ コカ・コーラ カンパニー | Beverages containing improved-taste salt |
| CN115611969B (en) * | 2021-07-14 | 2025-10-17 | 潍坊康地恩生物科技有限公司 | Soomasweet mutant and application thereof |
| EP4417699A4 (en) * | 2021-10-19 | 2025-12-24 | Cj Cheiljedang Corp | METHOD FOR THE PREPARATION OF REBAUDIOSIDE D AND REBAUDIOSIDE M |
| CN115558651B (en) * | 2021-12-30 | 2025-08-22 | 中化健康产业发展有限公司 | A glycosyltransferase CaUGT that catalyzes rebaudioside A to produce various steviol glycoside derivatives |
| CN114921431B (en) * | 2022-05-05 | 2023-04-25 | 湖北大学 | Glycosyltransferase mutant and application thereof in fermentation production of aromatic alcohol glycoside |
| CN114875054B (en) * | 2022-06-24 | 2023-11-17 | 南京工业大学 | A method for enzymatic preparation of glycosylated steviol glycoside compounds and their derivatives |
| WO2024042486A1 (en) | 2022-08-26 | 2024-02-29 | Amyris Bio Products Portugal, Unipessoal, Ltda. | Compositions and methods for the production of polyurethanes |
| WO2024042405A1 (en) | 2022-08-26 | 2024-02-29 | Amyris Bio Products Portugal, Unipessoal, Ltda. | Compositions and methods for the synthesis of bio-based polymers |
| CN118126977A (en) * | 2022-12-01 | 2024-06-04 | 南京工业大学 | A glycosyltransferase mutant and a method for catalyzing the synthesis of rubusoside derivative Rub2G |
| WO2024116153A1 (en) | 2022-12-02 | 2024-06-06 | Amyris Bio Products Portugal, Unipessoal, Ltda. | Compositions and methods for using previously cultured cells |
| CN116462777B (en) * | 2023-04-14 | 2023-11-17 | 桂林莱茵合成生物技术有限公司 | Novel glucosyl stevioside RMM and application and synthesis method thereof |
| WO2025001471A1 (en) * | 2023-06-30 | 2025-01-02 | 东台市浩瑞生物科技有限公司 | Glycosyltransferase ugtsl2 mutant, glycosyltransferase mutant, and method for synthesizing rebaudioside m2 therewith |
| CN117256832A (en) * | 2023-09-19 | 2023-12-22 | 领航食品(肇庆)有限公司 | Preparation method and application of mogroside |
| CN117717136B (en) * | 2024-02-05 | 2025-11-18 | 温州大学 | A sodium hyaluronate beverage, its preparation method and application |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090074935A1 (en) * | 2007-09-17 | 2009-03-19 | Pepsico, Inc. | Steviol glycoside isomers |
| US20110183056A1 (en) * | 2008-10-03 | 2011-07-28 | Toyoshige Morita | New steviol glycoside |
| US20110195161A1 (en) * | 2010-02-08 | 2011-08-11 | Coca Cola Company | Solubility enhanced terpene glycoside(s) |
| US8030481B2 (en) * | 2007-05-21 | 2011-10-04 | The Coca-Cola Company | Stevioside polymorphic and amorphous forms, methods for their formulation, and uses |
| US8299224B2 (en) * | 2009-10-15 | 2012-10-30 | Purecircle Sdn Bhd | High-purity Rebaudioside D |
| WO2013022989A2 (en) | 2011-08-08 | 2013-02-14 | Evolva Sa | Recombinant production of steviol glycosides |
| US20130078193A1 (en) * | 2011-09-22 | 2013-03-28 | Nutrinova Nutrition Specialties & Food Ingredients Gmbh | Sweetener Compositions, Methods of Making Same and Consumables Containing Same |
| US8414950B2 (en) * | 2009-10-15 | 2013-04-09 | Purecircle Sdn Bhd | High-purity rebaudioside D and low-calorie table top tablet containing the same |
| WO2013096420A1 (en) | 2011-12-19 | 2013-06-27 | The Coca-Cola Company | Methods for purifying steviol glycosides and uses of the same |
Family Cites Families (194)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3030481A (en) | 1957-12-23 | 1962-04-17 | S & C Electric Co | Switch construction |
| US3017168A (en) | 1959-01-26 | 1962-01-16 | Phillips Petroleum Co | In situ retorting of oil shale |
| US3723410A (en) | 1970-12-01 | 1973-03-27 | Amazon Natural Drug Co | Method of producing stevioside |
| JPS51142570A (en) | 1975-06-04 | 1976-12-08 | Morita Kagaku Kogyo | Method of imparting sweetness to food or pharmaceutical agent |
| JPS525800A (en) | 1975-06-27 | 1977-01-17 | Sanyo Kokusaku Pulp Co Ltd | Method of purifying stevioside |
| JPS5283731A (en) | 1976-01-01 | 1977-07-12 | Ajinomoto Co Inc | Rebaudiosides |
| JPS52100500A (en) | 1976-02-18 | 1977-08-23 | Japan Organo Co Ltd | Purification and concentration of aqueous stevioside extract |
| JPS52136200A (en) | 1976-05-12 | 1977-11-14 | Daicel Chem Ind Ltd | Extraction purification of stevioside |
| JPS5338669A (en) | 1976-09-16 | 1978-04-08 | Toyo Soda Mfg Co Ltd | Separation of natural sweetening agent |
| JPS5430199A (en) | 1977-08-08 | 1979-03-06 | Sanyo Kokusaku Pulp Co Ltd | Purification of stevia sweetening agnet |
| JPS54132599A (en) | 1978-04-04 | 1979-10-15 | Sanyo Kokusaku Pulp Co Ltd | Separation and purification of stevioside sweetening |
| US4219571A (en) | 1978-06-15 | 1980-08-26 | Kabushiki Kaisha Hayashibara Seibutsu Kagaku Kenkyujo | Process for producing a sweetener |
| JPS5539731A (en) | 1978-09-11 | 1980-03-19 | Res Inst For Prod Dev | Extraction of stevioside |
| JPS5581567A (en) | 1978-12-13 | 1980-06-19 | Res Inst For Prod Dev | Extraction and purification of stevioside |
| JPS5592400A (en) | 1978-12-29 | 1980-07-12 | Daikin Ind Ltd | Purification of stevioside |
| JPS55120770A (en) | 1979-03-14 | 1980-09-17 | Chisso Corp | Purification of stevioside solution |
| JPS55138372A (en) | 1979-04-13 | 1980-10-29 | Chisso Corp | Purification of stevioside solution |
| JPS55162953A (en) | 1979-06-04 | 1980-12-18 | Yamada Masami | Preparation of stevioside |
| JPS607108B2 (en) | 1979-11-13 | 1985-02-22 | 不二サッシ株式会社 | Curtain wall renovation method |
| JPS5699768A (en) | 1980-01-09 | 1981-08-11 | Hayashibara Biochem Lab Inc | Preparation of steviol glycoside |
| JPS56109568A (en) | 1980-02-01 | 1981-08-31 | Maruzen Kasei Kk | Purification of stevia sweetening substance |
| JPS56121454A (en) | 1980-02-27 | 1981-09-24 | Ajinomoto Co Inc | Separation of stevioside and rebaudioside a by crystallization |
| JPS56121455A (en) | 1980-02-27 | 1981-09-24 | Ajinomoto Co Inc | Separation of stevioside and rebaudioside a by crystallization |
| JPS56121453A (en) | 1980-02-27 | 1981-09-24 | Ajinomoto Co Inc | Separation of stevioside and rebaudioside a |
| JPS56160962A (en) | 1980-05-14 | 1981-12-11 | Dick Fine Chem Kk | Purification of solution containing stevioside-type sweetening substance |
| JPS55159770A (en) | 1980-05-26 | 1980-12-12 | Res Inst For Prod Dev | Extraction and purification of stevioside |
| JPS572656A (en) | 1980-06-05 | 1982-01-08 | Shinnakamura Kagaku Kogyo Kk | Decoloration and purification of stevia extract |
| JPS575663A (en) | 1980-06-13 | 1982-01-12 | Res Inst For Prod Dev | Purification of stevioside through extraction |
| JPS5746998A (en) | 1980-09-04 | 1982-03-17 | Fuji Food:Kk | Preparation of stevioside |
| US4454290A (en) | 1980-09-22 | 1984-06-12 | Dynapol | Stevioside analogs |
| JPS5775992A (en) | 1980-10-30 | 1982-05-12 | Tama Seikagaku Kk | Purification of stevioside |
| JPS5846310B2 (en) | 1980-11-19 | 1983-10-15 | 丸善化成株式会社 | How to isolate the main sweetening components in Stevia |
| JPS57134498A (en) | 1981-02-12 | 1982-08-19 | Hayashibara Biochem Lab Inc | Anhydrous crystalline maltitol and its preparation and use |
| US4361697A (en) | 1981-05-21 | 1982-11-30 | F. K. Suzuki International, Inc. | Extraction, separation and recovery of diterpene glycosides from Stevia rebaudiana plants |
| JPS5820170A (en) | 1981-07-24 | 1983-02-05 | Toshizo Fukushima | Preparation of sweetener |
| JPS5828247A (en) | 1981-08-10 | 1983-02-19 | Mitsubishi Acetate Co Ltd | Purification method of stevioside solution |
| JPS5828246A (en) | 1981-08-10 | 1983-02-19 | Mitsubishi Acetate Co Ltd | Preparation of stevioside |
| JPS58149697A (en) | 1982-02-27 | 1983-09-06 | Dainippon Ink & Chem Inc | Method for producing β-1,3 glycosyl stevioside |
| JPS58212760A (en) | 1982-06-04 | 1983-12-10 | Sekisui Chem Co Ltd | Purification of stevia sweetening substance |
| JPS58212759A (en) | 1982-06-04 | 1983-12-10 | Sekisui Chem Co Ltd | Purification of stevia sweetening substance |
| JPS5945848A (en) | 1982-09-09 | 1984-03-14 | Morita Kagaku Kogyo Kk | Novel natural sweetener |
| GB8403612D0 (en) * | 1984-02-10 | 1984-03-14 | Tate & Lyle Plc | Sweetener |
| US4612942A (en) | 1984-03-08 | 1986-09-23 | Stevia Company, Inc. | Flavor enhancing and modifying materials |
| US4657638A (en) | 1985-07-29 | 1987-04-14 | University Of Florida | Distillation column |
| US4599403A (en) | 1985-10-07 | 1986-07-08 | Harold Levy | Method for recovery of stevioside |
| JPS62166861A (en) | 1986-01-20 | 1987-07-23 | Sanpack:Kk | Extraction and purification of sweetener component from dry leaf of stevia |
| DE3788351D1 (en) | 1987-07-21 | 1994-01-13 | Roger H Giovanetto | Process for the production of steviosides from vegetable raw material. |
| JP3111203B2 (en) | 1987-12-26 | 2000-11-20 | 中里 隆憲 | Plants belonging to new Stevia varieties |
| DE3810681A1 (en) | 1988-03-29 | 1989-10-12 | Udo Kienle | METHOD FOR PRODUCING A NATURAL SWEETENER BASED ON STEVIA REBAUDIANA AND ITS USE |
| JP2898688B2 (en) | 1990-03-14 | 1999-06-02 | 日本製紙株式会社 | Highly sweetened sugar-added stevia sweetener and process for producing the same |
| CN1024348C (en) | 1990-05-23 | 1994-04-27 | 孟凡彬 | Process for extracting stevioside from ordinary resin |
| US5576042A (en) | 1991-10-25 | 1996-11-19 | Fuisz Technologies Ltd. | High intensity particulate polysaccharide based liquids |
| JPH067108A (en) | 1992-06-23 | 1994-01-18 | P C C Technol:Kk | Stevia sweet substance extraction and separation method |
| JPH06192283A (en) | 1992-12-17 | 1994-07-12 | Ikeda Pan:Kk | Method for production pure rebaudioside a |
| CN1032651C (en) | 1993-09-21 | 1996-08-28 | 袁斯鸣 | Method for refining stevioside |
| JP3436317B2 (en) | 1993-11-24 | 2003-08-11 | 大日本インキ化学工業株式会社 | Method for producing stevia sweetener |
| JPH07177862A (en) | 1993-12-24 | 1995-07-18 | Morita Kagaku Kogyo Kk | Slightly water-soluble sweetener |
| US5549757A (en) | 1994-06-10 | 1996-08-27 | Ingredient Technology Corporation | Process for recrystallizing sugar and product thereof |
| JPH08214A (en) | 1994-06-17 | 1996-01-09 | Ikeda Pan:Kk | Rebaudioside a-based sweetener and its production |
| JP3262458B2 (en) | 1994-07-29 | 2002-03-04 | キヤノン株式会社 | Recording device |
| CN1112565A (en) | 1995-03-06 | 1995-11-29 | 北京市环境保护科学研究院 | Process for extracting stevioside by membrane method combined technology |
| JP3352860B2 (en) | 1995-10-19 | 2002-12-03 | 守田化学工業株式会社 | α-Glucosylated Stevia sweetener |
| RU2111969C1 (en) | 1995-11-08 | 1998-05-27 | Республиканская научно-исследовательская лаборатория по биологически активным веществам | Method of stevioside preparing |
| US5962678A (en) * | 1996-09-13 | 1999-10-05 | Alberta Research Council | Method of extracting selected sweet glycosides from the Stevia rebaudiana plant |
| TW557327B (en) | 1996-11-08 | 2003-10-11 | Hayashibara Biochem Lab | Kojibiose phosphorylase, its preparation and uses |
| JP2002262822A (en) | 1997-01-30 | 2002-09-17 | Morita Kagaku Kogyo Kk | Sweetener obtained from plant body of variety of stevia rebaudiana cultivatable from seed |
| JPH10271928A (en) | 1997-01-30 | 1998-10-13 | Morita Kagaku Kogyo Kk | New plant belonging to stevia rabaudiana berton. |
| RU2156083C2 (en) | 1997-06-24 | 2000-09-20 | Дмитриенко Николай Васильевич | Method of obtaining extract from stevia grass |
| RU2123267C1 (en) | 1997-06-24 | 1998-12-20 | Дмитриенко Николай Васильевич | Method of preparing concentrate of extract from powder of stevia herb |
| JPH1131191A (en) | 1997-07-14 | 1999-02-02 | Olympus Optical Co Ltd | Multimedia information reader |
| US5972120A (en) | 1997-07-19 | 1999-10-26 | National Research Council Of Canada | Extraction of sweet compounds from Stevia rebaudiana Bertoni |
| JP3646497B2 (en) | 1997-12-22 | 2005-05-11 | 味の素株式会社 | Granular sweetener |
| CN1078217C (en) | 1998-02-18 | 2002-01-23 | 南开大学 | Adsorption resin method for conectrating and separating vegetable baudy glucoside from stevioside |
| GB9808579D0 (en) * | 1998-04-22 | 1998-06-24 | Novartis Nutrition Ag | Improvements in or relating to organic compounds |
| CN1098860C (en) | 1998-06-08 | 2003-01-15 | 江苏省中国科学院植物研究所 | Process for separating and concentrating high-quality stevioside |
| JP2000236842A (en) | 1998-12-24 | 2000-09-05 | Nippon Paper Industries Co Ltd | Stevia sweetener |
| US6228996B1 (en) | 1999-02-24 | 2001-05-08 | James H. Zhou | Process for extracting sweet diterpene glycosides |
| RU2167544C2 (en) | 1999-03-09 | 2001-05-27 | Краснодарский научно-исследовательский институт хранения и переработки сельскохозяйственной продукции | Method of preparing extract from plant stevia rebaudiana bertoni for winemaking |
| US20020132320A1 (en) | 2001-01-10 | 2002-09-19 | Wang Peng George | Glycoconjugate synthesis using a pathway-engineered organism |
| RU2198548C1 (en) | 2001-06-01 | 2003-02-20 | Общество с ограниченной ответственностью Научно-производственное холдинговое объединение "СТЕВИЯ-АГРОМЕДФАРМ" | Method of producing extract from plants stevia rebaudiana bertoni |
| CN1132840C (en) | 2001-10-24 | 2003-12-31 | 青岛创升生物科技有限公司 | Stevioside glycoside refining process |
| RU2315811C2 (en) | 2002-02-14 | 2008-01-27 | Новозимс А/С | Method for starch treatment |
| SE0200539D0 (en) | 2002-02-25 | 2002-02-25 | Metcon Medicin Ab | Granulation process and starch granulate |
| US6855526B2 (en) * | 2002-05-15 | 2005-02-15 | The United States Of America As Represented By The Secretary Of Agriculture | Method for making mannitol with Lactobacillus intermedius |
| CN1237182C (en) | 2002-06-25 | 2006-01-18 | 山东华仙甜菊股份有限公司 | Process for improving taste of ribaudiose |
| CN102613450A (en) | 2003-03-10 | 2012-08-01 | 金克克国际有限公司 | Grain compositions containing pre-biotic isomal to-oligosaccharides and methods of making and using same |
| BRPI0507583A (en) | 2004-03-17 | 2007-07-03 | Cargill Inc | low glycemic index sweeteners and products made using the same |
| US7476248B2 (en) | 2004-04-06 | 2009-01-13 | Alcon, Inc. | Method of calculating the required lens power for an opthalmic implant |
| CN101039688A (en) * | 2004-08-18 | 2007-09-19 | 生物健康解决方案股份有限公司 | Herbal composition for preventing or treating urinary incontinence and overactive bladder |
| US7923552B2 (en) | 2004-10-18 | 2011-04-12 | SGF Holdings, LLC | High yield method of producing pure rebaudioside A |
| US7838044B2 (en) | 2004-12-21 | 2010-11-23 | Purecircle Sdn Bhd | Extraction, separation and modification of sweet glycosides from the Stevia rebaudiana plant |
| US20060142555A1 (en) | 2004-12-23 | 2006-06-29 | Council Of Scientific And Industrial Research | Process for production of steviosides from stevia rebaudiana bertoni |
| WO2006072878A1 (en) | 2005-01-07 | 2006-07-13 | Ranbaxy Laboratories Limited | Oral dosage forms of sertraline having controlled particle size and processes for their preparation |
| WO2006072879A1 (en) | 2005-01-07 | 2006-07-13 | Ranbaxy Laboratories Limited | Preparation of sweetener tablets of stevia extract by dry granulation methods |
| US7838011B2 (en) | 2005-02-14 | 2010-11-23 | Pankaj Modi | Stabilized protein compositions for topical administration and methods of making same |
| US8613910B2 (en) * | 2005-07-27 | 2013-12-24 | Merck Patent Gmbh | Flavonoids as synergists for enhancing the action of self-tanning substances |
| US9386797B2 (en) | 2011-02-17 | 2016-07-12 | Purecircle Sdn Bhd | Glucosyl stevia composition |
| US8318459B2 (en) | 2011-02-17 | 2012-11-27 | Purecircle Usa | Glucosyl stevia composition |
| US7862845B2 (en) | 2005-10-11 | 2011-01-04 | Purecircle Sdn Bhd | Process for manufacturing a sweetener and use thereof |
| US8334006B2 (en) | 2005-10-11 | 2012-12-18 | Purecircle Sdn Bhd | Process for manufacturing a sweetener and use thereof |
| US8790730B2 (en) | 2005-10-11 | 2014-07-29 | Purecircle Usa | Process for manufacturing a sweetener and use thereof |
| US8298599B2 (en) | 2005-10-11 | 2012-10-30 | Purecircle Sdn Bhd | Process for manufacturing a sweetener and use thereof |
| US8257948B1 (en) | 2011-02-17 | 2012-09-04 | Purecircle Usa | Method of preparing alpha-glucosyl Stevia composition |
| US8318232B2 (en) | 2005-10-11 | 2012-11-27 | Purecircle Sdn Bhd | Sweetner and use |
| US8337927B2 (en) | 2005-10-11 | 2012-12-25 | Purecircle Sdn Bhd | Process for manufacturing a sweetener and use thereof |
| US7807206B2 (en) | 2005-10-11 | 2010-10-05 | Purecircle Sdn Bhd | Sweetner and use |
| US8956677B2 (en) | 2005-11-23 | 2015-02-17 | The Coca-Cola Company | High-potency sweetener composition with glucosamine and compositions sweetened therewith |
| US20070116829A1 (en) | 2005-11-23 | 2007-05-24 | The Coca-Cola Company | Pharmaceutical Composition with High-Potency Sweetener |
| US8435588B2 (en) | 2005-11-23 | 2013-05-07 | The Coca-Cola Company | High-potency sweetener composition with an anti-inflammatory agent and compositions sweetened therewith |
| US8524304B2 (en) | 2005-11-23 | 2013-09-03 | The Coca-Cola Company | High-potency sweetener composition with probiotics/prebiotics and compositions sweetened therewith |
| US9101160B2 (en) | 2005-11-23 | 2015-08-11 | The Coca-Cola Company | Condiments with high-potency sweetener |
| US8524303B2 (en) | 2005-11-23 | 2013-09-03 | The Coca-Cola Company | High-potency sweetener composition with phytosterol and compositions sweetened therewith |
| US20070116831A1 (en) | 2005-11-23 | 2007-05-24 | The Coca-Cola Company | Dental Composition with High-Potency Sweetener |
| US8945652B2 (en) | 2005-11-23 | 2015-02-03 | The Coca-Cola Company | High-potency sweetener for weight management and compositions sweetened therewith |
| US8367137B2 (en) | 2005-11-23 | 2013-02-05 | The Coca-Cola Company | High-potency sweetener composition with fatty acid and compositions sweetened therewith |
| US20070116833A1 (en) | 2005-11-23 | 2007-05-24 | The Coca-Cola Company | High-Potency Sweetener Composition with Calcium and Compositions Sweetened Therewith |
| US20070116800A1 (en) | 2005-11-23 | 2007-05-24 | The Coca-Cola Company | Chewing Gum with High-Potency Sweetener |
| US20070134391A1 (en) | 2005-11-23 | 2007-06-14 | The Coca-Cola Company | High-Potency Sweetener Composition for Treatment and/or Prevention of Autoimmune Disorders and Compositions Sweetened Therewith |
| US8367138B2 (en) | 2005-11-23 | 2013-02-05 | The Coca-Cola Company | Dairy composition with high-potency sweetener |
| US8993027B2 (en) | 2005-11-23 | 2015-03-31 | The Coca-Cola Company | Natural high-potency tabletop sweetener compositions with improved temporal and/or flavor profile, methods for their formulation, and uses |
| US8512789B2 (en) | 2005-11-23 | 2013-08-20 | The Coca-Cola Company | High-potency sweetener composition with dietary fiber and compositions sweetened therewith |
| US9144251B2 (en) | 2005-11-23 | 2015-09-29 | The Coca-Cola Company | High-potency sweetener composition with mineral and compositions sweetened therewith |
| US20070116836A1 (en) | 2005-11-23 | 2007-05-24 | The Coca-Cola Company | High-Potency Sweetener Composition for Treatment and/or Prevention of Osteoporosis and Compositions Sweetened Therewith |
| US20070116823A1 (en) | 2005-11-23 | 2007-05-24 | The Coca-Cola Company | High-potency sweetener for hydration and sweetened hydration composition |
| US8940350B2 (en) | 2005-11-23 | 2015-01-27 | The Coca-Cola Company | Cereal compositions comprising high-potency sweeteners |
| EP3199033B1 (en) | 2005-11-23 | 2020-10-07 | The Coca-Cola Company | Natural high-potency sweetener compositions with improved temporal profile and/or flavor profile, methods for their formulation, and uses |
| US8940351B2 (en) | 2005-11-23 | 2015-01-27 | The Coca-Cola Company | Baked goods comprising high-potency sweetener |
| US20070116825A1 (en) | 2005-11-23 | 2007-05-24 | The Coca-Cola Company | Confection with High-Potency Sweetener |
| US8956678B2 (en) | 2005-11-23 | 2015-02-17 | The Coca-Cola Company | High-potency sweetener composition with preservative and compositions sweetened therewith |
| US20070116839A1 (en) | 2005-11-23 | 2007-05-24 | The Coca-Cola Company | High-Potency Sweetener Composition With C-Reactive Protein Reducing Substance and Compositions Sweetened Therewith |
| US20070116822A1 (en) | 2005-11-23 | 2007-05-24 | The Coca-Cola Company | High-potency sweetener composition with saponin and compositions sweetened therewith |
| US8377491B2 (en) | 2005-11-23 | 2013-02-19 | The Coca-Cola Company | High-potency sweetener composition with vitamin and compositions sweetened therewith |
| US8435587B2 (en) | 2005-11-23 | 2013-05-07 | The Coca-Cola Company | High-potency sweetener composition with long-chain primary aliphatic saturated alcohol and compositions sweetened therewith |
| US20070116820A1 (en) | 2005-11-23 | 2007-05-24 | The Coca-Cola Company | Edible gel compositions comprising high-potency sweeteners |
| US8962058B2 (en) | 2005-11-23 | 2015-02-24 | The Coca-Cola Company | High-potency sweetener composition with antioxidant and compositions sweetened therewith |
| US7927851B2 (en) | 2006-03-21 | 2011-04-19 | Vineland Research And Innovation Centre | Compositions having ent-kaurenoic acid 13-hydroxylase activity and methods for producing same |
| US8791253B2 (en) | 2006-06-19 | 2014-07-29 | The Coca-Cola Company | Rebaudioside A composition and method for purifying rebaudioside A |
| US9012626B2 (en) | 2006-06-19 | 2015-04-21 | The Coca-Cola Company | Rebaudioside a composition and method for purifying rebaudioside a |
| CN101495642B (en) | 2006-08-11 | 2013-06-19 | 丹尼斯科美国公司 | Native grain amylases in enzyme combinations for granular starch hydrolysis |
| WO2008035701A1 (en) | 2006-09-20 | 2008-03-27 | Yuyama Mfg. Co., Ltd. | Medicine packaging apparatus |
| FR2906712B1 (en) | 2006-10-09 | 2025-02-28 | France Chirurgie Instr | SIMPLIFIED INSTALLATION METAL PLUG. |
| FR2906973B1 (en) | 2006-10-17 | 2009-01-16 | Roquette Freres | GRANULATED EDULCORING COMPOSITION |
| US20080102497A1 (en) | 2006-10-31 | 2008-05-01 | Dominic Wong | Enzymatic hydrolysis of starch |
| US20080107787A1 (en) | 2006-11-02 | 2008-05-08 | The Coca-Cola Company | Anti-Diabetic Composition with High-Potency Sweetener |
| US8017168B2 (en) | 2006-11-02 | 2011-09-13 | The Coca-Cola Company | High-potency sweetener composition with rubisco protein, rubiscolin, rubiscolin derivatives, ace inhibitory peptides, and combinations thereof, and compositions sweetened therewith |
| US9101161B2 (en) | 2006-11-02 | 2015-08-11 | The Coca-Cola Company | High-potency sweetener composition with phytoestrogen and compositions sweetened therewith |
| FI20070521L (en) | 2006-11-10 | 2008-05-11 | Atacama Labs Oy | Granules, tablets and granulation method |
| CN101200480B (en) | 2006-12-15 | 2011-03-30 | 成都华高药业有限公司 | Extraction method of rebaudioside A |
| ES2381892T3 (en) | 2007-01-22 | 2012-06-01 | Cargill, Incorporated | Process for producing purified rebaudioside A compositions using solvent / antisolvent crystallization |
| US9877500B2 (en) | 2007-03-14 | 2018-01-30 | Concentrate Manufacturing Company Of Ireland | Natural beverage products |
| BRPI0701736A (en) | 2007-04-05 | 2008-07-15 | Stevia Natus Produtos Naturais | physical-chemical industrial process of obtaining natural sweeteners and pure active principles of stevioside and rebaudioside a from stevia leaf without the use of organic solvents for the manufacture of sweeteners |
| EP3115452B1 (en) | 2007-04-26 | 2019-10-16 | Hayashibara Co., Ltd. | Branched alpha-glucan, alpha-glucosyltransferase which forms glucan, their preparation and uses |
| US20080292765A1 (en) | 2007-05-22 | 2008-11-27 | The Coca-Cola Company | Sweetness Enhancers, Sweetness Enhanced Sweetener Compositions, Methods for Their Formulation, and Uses |
| US8709521B2 (en) | 2007-05-22 | 2014-04-29 | The Coca-Cola Company | Sweetener compositions having enhanced sweetness and improved temporal and/or flavor profiles |
| US20080292775A1 (en) | 2007-05-22 | 2008-11-27 | The Coca-Cola Company | Delivery Systems for Natural High-Potency Sweetener Compositions, Methods for Their Formulation, and Uses |
| US20090017185A1 (en) | 2007-06-29 | 2009-01-15 | Catani Steven J | Stevia-containing tabletop sweeteners and methods of producing same |
| TWI475963B (en) | 2008-02-25 | 2015-03-11 | Coca Cola Co | Rebaudioside a derivative products and methods for making |
| FR2929533B1 (en) | 2008-04-03 | 2010-04-30 | Novasep | MULTICOLOUR GRADIENT SEPARATION PROCESS. |
| JP2011517686A (en) | 2008-04-11 | 2011-06-16 | ボード オブ スーパーバイザーズ オブ ルイジアナ ステイト ユニバーシティー アンド アグリカルチュラル アンド メカニカル カレッジ | Diterpene glycosides as natural solubilizers |
| US8321670B2 (en) | 2008-07-11 | 2012-11-27 | Bridgewater Systems Corp. | Securing dynamic authorization messages |
| WO2010057024A1 (en) | 2008-11-14 | 2010-05-20 | Cargill, Incorporated | Improving perceptional characteristics of beverages |
| US20120058236A1 (en) | 2009-04-09 | 2012-03-08 | Cargill Incorporated | Sweetener composition comprising high solubility form of rebaudioside a and method of making |
| ES2523997T3 (en) | 2009-06-16 | 2014-12-03 | Epc (Beijing) Natural Products Co., Ltd. | Reduction or elimination of residual flavor in a sweetener using rebaudioside D |
| MX2012003686A (en) | 2009-10-15 | 2012-07-25 | Purecircle Sdn Bhd | High-purity rebaudioside d and applications. |
| US8703224B2 (en) | 2009-11-04 | 2014-04-22 | Pepsico, Inc. | Method to improve water solubility of Rebaudioside D |
| US20110111115A1 (en) | 2009-11-06 | 2011-05-12 | Jingang Shi | Rebaudioside a polymorphs and methods to prepare them |
| US10004245B2 (en) | 2009-11-12 | 2018-06-26 | Purecircle Sdn Bhd | Granulation of a stevia sweetener |
| JP2013515492A (en) * | 2009-12-28 | 2013-05-09 | ザ コカ・コーラ カンパニー | Sweetness enhancer, composition containing sweetness enhancer, and methods of use thereof |
| US20110189360A1 (en) | 2010-02-04 | 2011-08-04 | Pepsico, Inc. | Method to Increase Solubility Limit of Rebaudioside D in an Aqueous Solution |
| BR122021005283B1 (en) | 2010-06-02 | 2022-02-22 | Evolva, Inc | RECOMBINANT HOST COMPRISING RECOMBINANT GENES FOR PRODUCTION OF STEVIOL OR STEVIOL GLYCOSIDE, METHOD FOR PRODUCING STEVIOL, STEVIOL GLYCOSIDE OR STEVIOL GLYCOSIDE COMPOSITION AND METHOD FOR SYNTHESISTING STEVIOL OR STEVIOL GLYCOSIDE |
| CA2819253A1 (en) | 2010-11-30 | 2012-06-07 | Massachusetts Institute Of Technology | Microbial production of natural sweeteners, diterpenoid steviol glycosides |
| BR112013014614B1 (en) | 2010-12-13 | 2019-07-16 | Cargill, Incorporated | Sweetener Composition Understanding a Glycoside Mixture |
| WO2012082493A1 (en) | 2010-12-13 | 2012-06-21 | Cargill, Incorporated | Crystalline forms of rebaudioside b |
| EP2657220B1 (en) | 2010-12-24 | 2016-08-31 | Daicel Corporation | Acetic acid production method |
| US9603373B2 (en) | 2011-02-17 | 2017-03-28 | Purecircle Sdn Bhd | Glucosyl stevia composition |
| CN103159808B (en) | 2011-12-09 | 2017-03-29 | 上海泓博智源医药股份有限公司 | A kind of process for preparing natural sweetener |
| EA201400836A8 (en) * | 2012-01-23 | 2016-03-31 | ДСМ АйПи АССЕТС Б.В. | OBTAINING Diterpen |
| US9752174B2 (en) * | 2013-05-28 | 2017-09-05 | Purecircle Sdn Bhd | High-purity steviol glycosides |
| MX395285B (en) * | 2012-05-22 | 2025-03-25 | Purecircle Sdn Bhd | HIGH PURITY STEVIOL GLUCOSIDES. |
| CN102766667B (en) * | 2012-08-14 | 2014-06-11 | 成都南诺格生物科技有限责任公司 | Method for transforming stevioside into rebaudioside E |
| JP6192283B2 (en) | 2012-10-11 | 2017-09-06 | スリーエム イノベイティブ プロパティズ カンパニー | Fastener parts |
| US20140122227A1 (en) * | 2012-10-25 | 2014-05-01 | Microsoft Corporation | Targeting marketing messages based on user preferences |
| CN105051195B (en) | 2013-02-06 | 2019-09-06 | 埃沃尔瓦公司 | Method for increasing the production of Rebaudioside D and Rebaudioside M |
| MX2015010098A (en) | 2013-02-11 | 2016-04-19 | Evolva Sa | Efficient production of steviol glycosides in recombinant hosts. |
| US20140342044A1 (en) * | 2013-05-14 | 2014-11-20 | Pepsico, Inc. | Compositions and Comestibles |
| US10952458B2 (en) | 2013-06-07 | 2021-03-23 | Purecircle Usa Inc | Stevia extract containing selected steviol glycosides as flavor, salty and sweetness profile modifier |
| EP3024941B1 (en) | 2013-07-23 | 2019-07-03 | DSM IP Assets B.V. | Diterpene production in yarrowia |
| CN103397064B (en) | 2013-08-14 | 2015-04-15 | 苏州汉酶生物技术有限公司 | Method for preparing rebaudioside M through enzyme method |
| US20170055554A1 (en) * | 2014-02-24 | 2017-03-02 | Suntory Beverage & Food Limited | Carbonated beverage containing high-intensity sweetener |
| US9522929B2 (en) | 2014-05-05 | 2016-12-20 | Conagen Inc. | Non-caloric sweetener |
| MX389746B (en) * | 2014-09-19 | 2025-03-20 | Purecircle Sdn Bhd | High-purity steviol glycosides |
| CN105200098A (en) | 2015-06-30 | 2015-12-30 | 苏州汉酶生物技术有限公司 | Method for preparing rebaudioside M according to saccharomyces cerevisiae enzymatic method |
| EP3725834A4 (en) | 2017-12-15 | 2021-02-24 | NEC Corporation | CELLULOSE-BASED RESIN COMPOSITION, MOLDED BODY, PRODUCT OBTAINED THEREFOR, AND PROCESS FOR PREPARING A CELLULOSE-BASED RESIN COMPOSITION |
| JP7177862B2 (en) | 2021-01-04 | 2022-11-24 | 本田技研工業株式会社 | positioning device |
-
2014
- 2014-05-27 US US14/287,837 patent/US9752174B2/en active Active
- 2014-05-28 WO PCT/US2014/039758 patent/WO2014193934A1/en not_active Ceased
- 2014-05-28 CN CN202011020696.6A patent/CN112538512A/en active Pending
- 2014-05-28 US US14/894,084 patent/US20160198748A1/en not_active Abandoned
- 2014-05-28 MX MX2015016362A patent/MX365044B/en active IP Right Grant
- 2014-05-28 CN CN201480036885.9A patent/CN105408339B/en active Active
- 2014-05-28 CN CN202011020773.8A patent/CN112626154B/en active Active
- 2014-05-28 CA CA2913252A patent/CA2913252C/en active Active
- 2014-05-28 WO PCT/US2014/039666 patent/WO2014193888A1/en not_active Ceased
- 2014-05-28 EP EP14804387.0A patent/EP3004128A4/en active Pending
- 2014-05-28 CA CA3089783A patent/CA3089783C/en active Active
- 2014-05-28 EP EP14804243.5A patent/EP3004127A4/en active Pending
- 2014-05-28 MX MX2015016096A patent/MX384819B/en unknown
- 2014-05-28 BR BR112015030082A patent/BR112015030082A2/en not_active Application Discontinuation
- 2014-05-28 MX MX2019005688A patent/MX395693B/en unknown
- 2014-05-28 CN CN201480040130.6A patent/CN105492453B/en active Active
- 2014-05-28 BR BR112015029684-0A patent/BR112015029684B1/en active IP Right Grant
-
2015
- 2015-11-23 MX MX2021008960A patent/MX2021008960A/en unknown
-
2017
- 2017-09-01 US US15/694,524 patent/US10683526B2/en active Active
-
2018
- 2018-03-21 US US15/927,538 patent/US11312984B2/en active Active
-
2020
- 2020-06-16 US US16/903,369 patent/US11542537B2/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8030481B2 (en) * | 2007-05-21 | 2011-10-04 | The Coca-Cola Company | Stevioside polymorphic and amorphous forms, methods for their formulation, and uses |
| US20090074935A1 (en) * | 2007-09-17 | 2009-03-19 | Pepsico, Inc. | Steviol glycoside isomers |
| US20110183056A1 (en) * | 2008-10-03 | 2011-07-28 | Toyoshige Morita | New steviol glycoside |
| US8299224B2 (en) * | 2009-10-15 | 2012-10-30 | Purecircle Sdn Bhd | High-purity Rebaudioside D |
| US8414950B2 (en) * | 2009-10-15 | 2013-04-09 | Purecircle Sdn Bhd | High-purity rebaudioside D and low-calorie table top tablet containing the same |
| US20110195161A1 (en) * | 2010-02-08 | 2011-08-11 | Coca Cola Company | Solubility enhanced terpene glycoside(s) |
| WO2013022989A2 (en) | 2011-08-08 | 2013-02-14 | Evolva Sa | Recombinant production of steviol glycosides |
| US20130078193A1 (en) * | 2011-09-22 | 2013-03-28 | Nutrinova Nutrition Specialties & Food Ingredients Gmbh | Sweetener Compositions, Methods of Making Same and Consumables Containing Same |
| WO2013096420A1 (en) | 2011-12-19 | 2013-06-27 | The Coca-Cola Company | Methods for purifying steviol glycosides and uses of the same |
Non-Patent Citations (2)
| Title |
|---|
| "Genbank", Database accession no. XP_002865752.1 |
| See also references of EP3004127A4 |
Cited By (65)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US12479877B2 (en) | 2010-03-12 | 2025-11-25 | The Coca-Cola Company | Methods for purifying steviol glycosides and uses of the same |
| US11155570B2 (en) | 2010-03-12 | 2021-10-26 | Purecircle Usa Inc. | Methods of preparing steviol glycosides and uses of the same |
| US12037356B2 (en) | 2010-03-12 | 2024-07-16 | Purecircle Usa Inc. | Methods of preparing steviol glycosides and uses of the same |
| US10696706B2 (en) | 2010-03-12 | 2020-06-30 | Purecircle Usa Inc. | Methods of preparing steviol glycosides and uses of the same |
| US11773125B2 (en) | 2010-03-12 | 2023-10-03 | Purecircle Usa Inc. | Methods of preparing steviol glycosides and uses of the same |
| US10602762B2 (en) | 2011-02-17 | 2020-03-31 | Purecircle Sdn Bhd | Glucosylated steviol glycoside as a flavor modifier |
| US12279635B2 (en) | 2011-02-17 | 2025-04-22 | PureCirlce Sdn. Bhd. | Glucosylated steviol glycoside as a flavor |
| US10743572B2 (en) | 2011-02-17 | 2020-08-18 | Purecircle Sdn Bhd | Glucosylated steviol glycoside as a flavor modifier |
| US11957144B2 (en) | 2011-02-17 | 2024-04-16 | Purecircle Sdn Bhd | Glucosylated steviol glycoside as a flavor modifier |
| US11690391B2 (en) | 2011-02-17 | 2023-07-04 | Purecircle Sdn Bhd | Glucosylated steviol glycoside as a flavor modifier |
| US9771434B2 (en) | 2011-06-23 | 2017-09-26 | Purecircle Sdn Bhd | Products from stevia rebaudiana |
| US11279773B2 (en) | 2011-06-23 | 2022-03-22 | Purecircle Sdn Bhd | Products from Stevia rabaudiana |
| EP2793618B1 (en) | 2011-12-19 | 2017-11-15 | The Coca-Cola Company | Beverage comprising steviol glycosides |
| EP3345490B1 (en) | 2011-12-19 | 2023-11-08 | The Coca-Cola Company | Beverage comprising rebaudioside x |
| EP2793618A1 (en) | 2011-12-19 | 2014-10-29 | The Coca-Cola Company | Methods for purifying steviol glycosides and uses of the same |
| US12441753B2 (en) | 2011-12-19 | 2025-10-14 | Purecircle Sdn. Bhd. | Methods for purifying steviol glycosides and uses of the same |
| US11957756B2 (en) | 2013-06-07 | 2024-04-16 | Purecircle Sdn Bhd | Stevia extract containing selected steviol glycosides as flavor, salty and sweetness profile modifier |
| US12011017B2 (en) | 2013-06-07 | 2024-06-18 | Purecircle Usa Inc. | Stevia extract containing selected steviol glycosides as flavor, salty and sweetness profile modifier |
| US10952458B2 (en) | 2013-06-07 | 2021-03-23 | Purecircle Usa Inc | Stevia extract containing selected steviol glycosides as flavor, salty and sweetness profile modifier |
| US10780170B2 (en) | 2013-06-07 | 2020-09-22 | Purecircle Sdn Bhd | Stevia extract containing selected steviol glycosides as flavor, salty and sweetness profile modifier |
| US11856972B2 (en) | 2014-09-02 | 2024-01-02 | Purecircle Sdn Bhd | Stevia extracts |
| US11230567B2 (en) | 2014-09-02 | 2022-01-25 | Purecircle Usa Inc. | Stevia extracts enriched in rebaudioside D, E, N and/or O and process for the preparation thereof |
| US11202461B2 (en) | 2014-09-02 | 2021-12-21 | Purecircle Sdn Bhd | Stevia extracts |
| US10711024B2 (en) | 2014-12-17 | 2020-07-14 | Cargill, Incorporated | Steviol glycoside compounds, compositions for oral ingestion or use, and method for enhancing steviol glycoside solubility |
| US10906927B2 (en) | 2014-12-17 | 2021-02-02 | Cargill, Incorporated | Steviol glycoside compounds, compositions for oral ingestion or use, and method for enhancing steviol glycoside solubility |
| US12030905B2 (en) | 2014-12-17 | 2024-07-09 | Carghill, Incorporated | Steviol glycoside compounds, compositions for oral ingestion or use, and method for enhancing steviol glycoside solubility |
| US11407780B2 (en) | 2014-12-17 | 2022-08-09 | Cargill, Incorporated | Steviol glycoside compounds, compositions for oral ingestion or use, and method for enhancing steviol glycoside solubility |
| US11344051B2 (en) | 2015-04-03 | 2022-05-31 | Dsm Ip Assets B.V. | Steviol glycosides |
| US11540544B2 (en) | 2015-04-03 | 2023-01-03 | Dsm Ip Assets B.V. | Steviol glycosides |
| WO2016196368A1 (en) | 2015-05-29 | 2016-12-08 | Cargill, Incorporated | Fermentation methods for producing steviol glycosides with multi-phase feeding |
| EP4134442A1 (en) | 2015-05-29 | 2023-02-15 | Cargill, Incorporated | Fermentation methods for producing steviol glycosides using high ph |
| US11028423B2 (en) | 2015-05-29 | 2021-06-08 | Cargill, Incorporated | Heat treatment to produce glycosides |
| US11225678B2 (en) | 2015-05-29 | 2022-01-18 | Cargill, Incorporated | Fermentation methods for producing steviol glycosides with multi-phase feeding |
| US10612065B2 (en) | 2015-05-29 | 2020-04-07 | Cargill, Incorporated | Heat treatment to produce glycosides |
| US11761022B2 (en) | 2015-05-29 | 2023-09-19 | Cargill, Incorporated | Heat treatment to produce glycosides |
| US11739353B2 (en) | 2015-05-29 | 2023-08-29 | Cargill, Incorporated | Fermentation methods for producing steviol glycosides with multi-phase feeding |
| US10815513B2 (en) | 2015-05-29 | 2020-10-27 | Cargill, Incorporated | Fermentation methods for producing steviol glycosides using high pH and compositions obtained therefrom |
| WO2016196321A1 (en) | 2015-05-29 | 2016-12-08 | Cargill, Incorporated | Fermentation methods for producing steviol glycosides using high ph and compositions obtained therefrom |
| EP4063513A1 (en) | 2015-05-29 | 2022-09-28 | Cargill, Incorporated | Heat treatment to produce glycosides |
| WO2016196345A1 (en) | 2015-05-29 | 2016-12-08 | Cargill, Incorporated | Heat treatment to produce glycosides |
| US10844414B2 (en) | 2015-08-06 | 2020-11-24 | Cargill, Incorporated | Methods for producing steviol glycosides in engineered yeast |
| US11647771B2 (en) | 2015-10-26 | 2023-05-16 | Purecircle Usa Inc. | Steviol glycoside compositions |
| US11653686B2 (en) | 2015-12-15 | 2023-05-23 | Purecircle Usa Inc. | Steviol glycoside compositions |
| US10815514B2 (en) | 2016-05-16 | 2020-10-27 | Evolva Sa | Production of steviol glycosides in recombinant hosts |
| US12371677B2 (en) | 2016-08-12 | 2025-07-29 | Corn Products Development, Inc. | UDP-dependent glycosyltransferase for high efficiency production of rebaudiosides |
| US11091743B2 (en) | 2016-08-12 | 2021-08-17 | Amyris, Inc. | UDP-dependent glycosyltransferase for high efficiency production of rebaudiosides |
| KR102331018B1 (en) | 2016-08-12 | 2021-11-26 | 아미리스 인코퍼레이티드 | UDP-dependent glycosyltransferase for high-efficiency production of rebaudioside |
| WO2018031955A2 (en) | 2016-08-12 | 2018-02-15 | Amyris, Inc. | Udp-dependent glycosyltransferase for high efficiency production of rebaudiosides |
| CN109804073B (en) * | 2016-08-12 | 2023-05-16 | 阿迈瑞斯公司 | UDP-dependent glycosyltransferase for efficient rebaudioside production |
| CN109804073A (en) * | 2016-08-12 | 2019-05-24 | 阿迈瑞斯公司 | For efficiently producing the UDP dependence glycosyl transferase of rebaudioside |
| US11866738B2 (en) | 2016-08-12 | 2024-01-09 | Amyris, Inc. | UDP-dependent glycosyltransferase for high efficiency production of rebaudiosides |
| KR20190038612A (en) * | 2016-08-12 | 2019-04-08 | 아미리스 인코퍼레이티드 | UDP-dependent glycosyltransferase for high-throughput production of rebaudioside |
| WO2018031955A3 (en) * | 2016-08-12 | 2018-03-15 | Amyris, Inc. | Udp-dependent glycosyltransferase for high efficiency production of rebaudiosides |
| JP2019536444A (en) * | 2016-10-21 | 2019-12-19 | ペプシコ・インク | Method for preparing rebaudioside J using an enzymatic method |
| US11952604B2 (en) | 2016-10-21 | 2024-04-09 | Pepsico, Inc. | Enzymatic method for preparing Rebaudioside J |
| WO2019033064A1 (en) | 2017-08-11 | 2019-02-14 | Amyris, Inc. | Pisum sativum kaurene oxidase for high efficiency production of rebaudiosides |
| JP2022501309A (en) * | 2018-09-29 | 2022-01-06 | フイルメニツヒ ソシエテ アノニムFirmenich Sa | Terpene glycoside derivatives and their use |
| WO2020081468A1 (en) | 2018-10-15 | 2020-04-23 | Amyris, Inc. | Stevia rebaudiana kaurenoic acid hydroxylase variants for high efficiency production of rebaudiosides |
| WO2020154549A2 (en) | 2019-01-24 | 2020-07-30 | Amyris, Inc. | Abc transporters for the high efficiency production of rebaudiosides |
| US12065685B1 (en) | 2019-05-13 | 2024-08-20 | Amyris, Inc. | UDP-glycosyltransferase variants and uses thereof |
| US12460239B2 (en) | 2019-05-13 | 2025-11-04 | Corn Products Development, Inc. | UDP-glycosyltransferase variants and uses thereof |
| JP7210626B2 (en) | 2021-02-18 | 2023-01-23 | ペプシコ・インク | Method for preparing rebaudioside J using enzymatic methods |
| JP2021087439A (en) * | 2021-02-18 | 2021-06-10 | ペプシコ・インク | Method for preparing rebaudioside j using enzymatic method |
| WO2022187819A1 (en) | 2021-03-01 | 2022-09-09 | Cargill, Incorporated | Xylosylated steviol glycosides and enzymatic methods for production |
| WO2024228615A1 (en) | 2023-05-03 | 2024-11-07 | Purecircle Sdn. Bhd. | High-purity steviol glycosides |
Also Published As
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US11542537B2 (en) | High-purity steviol glycosides | |
| US11653679B2 (en) | High-purity steviol glycosides | |
| US20250263768A1 (en) | High-purity steviol glycosides | |
| JP2024040374A (en) | High purity steviol glycoside | |
| AU2019282411B2 (en) | High-purity steviol glycosides | |
| KR20210125474A (en) | High Purity Steviol Glycoside | |
| KR20210129679A (en) | High Purity Steviol Glycoside | |
| AU2019236227B2 (en) | High-purity steviol glycosides | |
| US20230413865A1 (en) | High-purity steviol glycosides | |
| US20240076708A1 (en) | High-purity steviol glycosides |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| WWE | Wipo information: entry into national phase |
Ref document number: 201480036885.9 Country of ref document: CN |
|
| 121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 14804243 Country of ref document: EP Kind code of ref document: A1 |
|
| WWE | Wipo information: entry into national phase |
Ref document number: MX/A/2015/016362 Country of ref document: MX |
|
| NENP | Non-entry into the national phase |
Ref country code: DE |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 122021004167 Country of ref document: BR |
|
| REG | Reference to national code |
Ref country code: BR Ref legal event code: B01A Ref document number: 112015030082 Country of ref document: BR |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 2014804243 Country of ref document: EP |
|
| ENP | Entry into the national phase |
Ref document number: 112015030082 Country of ref document: BR Kind code of ref document: A2 Effective date: 20151130 |