High yield method of producing pure rebaudioside A
AssigneeSGF Holdings, LLC
InventorsMel Clinton Jackson, Gordon James Francis, Robert Gordon Chase
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AssigneeSGF Holdings, LLC
InventorsMel Clinton Jackson, Gordon James Francis, Robert Gordon Chase
Estimating the term…
The invention provides a high throughput, high purity, high yield system and method of isolating and purifying rebaudioside A (“Reb A”), with acceptable water solubility for all commercial uses, from commercially available Stevia rebaudiana starting material. The invention also provides a means of maximizing yields of 99+% purity Reb A based on the attributes of a given batch of Stevia starting material. The Reb A produced by the invention is water soluble, devoid of bitterness heretofore associated with rebaudioside sweeteners, non-caloric, and suitable for use as a reagent and as an ingredient in orally consumed products, e.g., as a sweetener, flavor enhancer, and flavor modifier.
A method of purifying rebaudioside A from Stevia starting material comprising:
A method of purifying rebaudioside A from Stevia starting material comprising:
A method of purifying rebaudioside A from Stevia starting material comprising:
A method of purifying rebaudioside A from Stevia starting material comprising:
A method of purifying rebaudioside A from Stevia starting material comprising:
A method of purifying rebaudioside A from Stevia starting material comprising:
Dependencies are inferred from the claim text.
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Condensed ring systems having three or more rings: naphthacene radicals, e.g. daunomycins, adriamycins
Containing sugars or derivatives: terpene glycosides
Drugs for disorders of the metabolism: anorexiants; Antiobesity agents
For glucose homeostasis: for hyperglycaemia, e.g. antidiabetics
About 2 years 7 months of term left · ends 23 May 2029 (estimated)
1. Technical Field
The invention is in the technical field of the purification of rebaudioside A (also known herein as “Reb A” and “RA”) from crude extracts from the plant Stevia rebaudiana, L. Bertoni (“Stevia”). Reb A is a diterpene glycoside found, along with many other glycosides, sterebins, and other compounds, in Stevia extracts. Reb A is the sweetest tasting (roughly 250 to 450 times the sweetness of sucrose at sweetener concentrations used in comestibles) glycoside in Stevia and has enormous commercial potential as a non-caloric sweetener. Generally speaking, the Stevia glycosides, except rebaudioside A, have an undesirable aftertaste (some have a bitter aftertaste), which generally limits the use of such non-Reb A glycosides as sweeteners. Moreover, sterebins (a group of diterpene compounds commonly known as “yellow oil”) in Stevia extracts have an extremely bitter taste, even in minute concentrations. In short, the technical field, and the technical problem, is to isolate, especially at industrial scale, 99+% purity Reb A from crude Stevia extract; such purity eliminates the bitterness or off-taste that characterizes all currently available Stevia sweeteners.
2. Related Art
FIG. 1 shows an overall view of the laboratory embodiment of the invention.
FIG. 2 shows the steps in the reflux stage of the laboratory process.
FIG. 3 shows the steps in the stirred wash stage of the laboratory process.
The invention comprises (i) a high purity, high yield laboratory process that provides 100% pure rebaudioside A using Stevia starting material; (ii) a high throughput, high purity, high yield industrial process, derived directly from the laboratory process, that provides commercial quantities of 99+% purity rebaudioside A using Stevia starting material; (iii) the rebaudioside A made by those processes; (iv) uses of such rebaudioside A; and (v) a means of maximizing yields of a target purity of Reb A based on the attributes of a given lot of Stevia starting material.
The utility of the laboratory process lies in the ability to produce 100% pure, water soluble Reb A for research, analytic, and synthetic purposes. The utility of the industrial process lies in the ability to produce commercial quantities (e.g., thousands of kilograms) of 99+% purity Reb A for the beverage, food, baking, candy, personal care product, pharmaceutical, tobacco, and other industries, as well as for research, analytics, and synthesis. As a result of the perceived sweetness of very low concentrations of pure Reb A, for most uses, including beverages, Reb A water solubility of less than 1% is acceptable (concentrates require higher solubility, but within the final product solubility range provided by the invention).
Reb A is significantly less expensive to produce using the invention compared with existing processes, even though the invention produces Reb A of far higher purity. The means provided herein of maximizing yields of 99+% purity Reb A based on the attributes of a given lot of Stevia starting material enables even greater savings in production costs compared with existing processes. Stevia starting material with greater than 40% purity Reb A content is preferred for use with the invention; the additional reflux stages typically required for Stevia starting material of less than RA40 quality typically make the process financially disfavored, and Stevia starting materials with greater than 40% purity Reb A are readily available. RA40 and higher Stevia starting materials are available from Shandong Chengwu Aoxing Stevia Production Co., Ltd., Datianji Town, Chengwu County, Shandong, People's Republic of China, as well as other sources known in the art. Stevia starting materials typically do not exceed RA80; however, a few commercially available, significantly more expensive Stevia extracts, such as the one sold under the product name of Rebaudio by Morita Kagaku Kogyou, Ltd., Joto-ku, Osaka, Japan, have approximately 90% Reb A content. In the reflux and stirred wash stages of the present invention, denatured ethanol is typically preferred for cost reasons, particularly for the industrial embodiment of the invention; absolute ethanol is approximately ten times as expensive as denatured ethanol in the U.S., but in locales where both denatured and absolute ethanol have substantially the same cost, absolute ethanol is preferred over denatured ethanol for use as a sole solvent and as a reflux solvent component. Denatured ethanol containing additives other than 1% ethyl acetate (e.g., ethanol denatured with 5% isopropanol) can be used in the invention, but typically result in reduced yields and purity of final product. Alkanols other than ethanol can be used, but using ethanol avoids food safety issues related to other alkanols.