IP Library Granted Patent US 10,480,019
Granted Patent B2
US 10,480,019 · App. 14/560,403 · Granted Nov 19, 2019

Process for producing high-purity rubusoside

Inventor: Avetik Markosyan (Yerevan, AM)
Assignee: PureCircle Sdn Bhd
C12P19/44A23L27/33A23L27/36A24B15/10C12P19/14C12P19/56
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Quick Facts
Patent No.
US 10,480,019
App. No.
14/560,403
Granted
Nov 19, 2019
Kind
B2
Abstract

The invention provides a process of producing Rubusoside from steviol glycosides of Stevia rebaudiana plant. The process is useful for producing high purity Rubusoside with purity greater than 95% (dry basis). High purity rubusoside is useful as in combination with other caloric and non-caloric sweeteners as well as non-caloric sweetener in various food and beverage compositions. The high purity rubusoside is useful as non-caloric sweetener in edible and chewable compositions such as any beverages, confectionaries, bakeries, cookies, chewing gums, and alike.

Claims (34)

1. A process for preparing Rubusoside from steviol glycosides of Stevia rebaudiana comprising the steps of:

A) providing a solution comprising Stevioside;

B) adding 2000 fungal β-glucanase (FBG) units of an enzyme composition having fungal β-glucanase activity to the solution comprising Stevioside to obtain a reaction mixture; and

C) incubating the reaction mixture at 28-50° C. for 12-48 hours to facilitate transformation of Stevioside to Rubusoside to obtain a reaction mixture containing Rubusoside.

2. The process of claim 1 wherein in step A) the concentration of Stevioside is 1-50% (wt/vol).

3. The process of claim 1 wherein in step C) the molar yield of Rubusoside from Stevioside is 1-100%.

4. The process of claim 1 further comprising:

D) at least one purification technique employed on the reaction mixture containing Rubusoside, selected from the group comprising ion exchange treatment, macroporous adsorbent treatment, membrane process, chromatographic separation, and crystallization from various solvent systems to obtain a purified Rubusoside.

5. The process of claim 1 further comprising:

D) recovery and purification of Rubusoside comprising the steps of:

a) providing the reaction mixture containing Rubusoside;

b) contacting the reaction mixture containing Rubusoside with macroporous adsorbent resin;

c) eluting the adsorbed Rubusoside with aqueous alcohol to obtain an eluate;

d) removing the alcohol from the eluate and drying the eluate to yield the purified Rubusoside.

6. The process of claim 1 further comprising:

D) recovery and purification of Rubusoside comprising the steps of:

a) providing a dried reaction mixture containing Rubusoside;

b) dissolving the dried reaction mixture in a first aqueous alcoholic solution to obtain a first mixture;

c) inducing crystallization in the first mixture by temperature gradient treatment;

d) filtering the first mixture to obtain a first precipitate and a first filtrate;

e) dissolving the first precipitate in a second aqueous alcoholic solution to obtain a second mixture;

f) adding activated carbon to the second mixture and filtering it to obtain a decolorized second mixture;

g) inducing crystallization in the decolorized second mixture by temperature gradient treatment;

h) filtering the decolorized second mixture to obtain a second precipitate and a second filtrate;

i) suspending the second precipitate in a third aqueous alcoholic solution to obtain a third mixture;

j) filtering the third mixture to obtain a third precipitate and a third filtrate; and

k) a drying the third precipitate to yield the purified Rubusoside.

7. The process of claim 6 wherein the first aqueous alcoholic solution in step b) is a methanol-water solution, with 75-99% methanol.

8. The process of claim 6 wherein the second aqueous alcoholic solution in step e) is a methanol-water solution with 70-90% methanol.

9. The process of claim 6 wherein the third aqueous alcoholic solution in step i) is a methanol-water solution with 90-99% methanol.

10. The process of claim 6 wherein steps c) and g) inducing crystallization comprises increasing the mixture temperature to 65-70° C. then gradually cooling it to 0-40° C., at a rate of 1-20° C. per hour with continuous mild agitation.

11. The process of claim 6 wherein the aqueous alcoholic solution comprises one or more organic solvents selected from the group consisting of methanol, ethanol, 1-propanol, and isopropanol.

12. The process of claim 1 , wherein the purified Rubusoside has a purity greater than 95% on a dry basis.

13. The process of claim 1 , wherein the purified Rubusoside has a purity greater than 98% on a dry basis.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 19, 2017
From: MARKOSYAN, AVETIK
To: PURECIRCLE SDN BHD
Reel/Frame 042884/0984 →
Continuity (6)
Continuation In Part 14380071
Continuation In Part 14560403
Continuation In Part 13553820 · Jul 20, 2012
Provisional Application 61608110 · Mar 8, 2012
Provisional Application 61522237 · Aug 10, 2011
Related Publication 20150118379A1 · Apr 30, 2015