IP Library Granted Patent US 8,461,360
Granted Patent B2
US 8,461,360 · App. 12/863,514 · Granted Jun 11, 2013

Process for producing γ -mangostin

Inventors: Ganga Raju Gokaraju (Vijayawada, IN); Rama Raju Gokaraju (Vijayawada, IN); Trimurtulu Golakoti (Vijayawada, IN); Venkateswarlu Somepalli (Vijayawada, IN); Kiran Bhupathiraju (Vijayawada, IN)
Assignee: Laila Nutraceuticals
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Quick Facts
Patent No.
US 8,461,360
App. No.
12/863,514
Granted
Jun 11, 2013
Kind
B2
Abstract

A process for the production of γ-mangostin comprising the steps of preparing O-methyl γ-mangostin preferably from plants, subjecting the pure or partially pure O-methylated γ-mangostin to demethylation reaction procedure followed by purification of the said demethylated product to obtain pure γ-mangostin.

Claims (56)

1. A process for producing γ-mangostin from at least one O-methyl xanthone of general formula I, wherein each of R 1 , R 2 , R 3 , and R 4 is either H or CH 3 , with the proviso that at least one of R 1 , R 2 , R 3 , and R 4 is CH 3 ;

said process comprising the steps of:

(i) subjecting said at least one O-methyl xanthone to a demethylation reaction using a demethylating reagent, and

(ii) purifying the said reaction product to obtain pure γ-mangostin;

wherein the demethylating reagent comprises an organic base and a Lewis acid.

2. The process as claimed in claim 1 , wherein said Lewis acid is selected from the group consisting of aluminum chloride, aluminum bromide, aluminum iodide, boron tribromide, boron trichloride-methyl sulfide complex, boron trichloride, boron trifluoride, zinc chloride and iron chloride.

3. The process as claimed in claim 1 , wherein the demethylating reagent is used with a catalyst, said catalyst being:

a metal iodide selected from the group consisting of sodium iodide, potassium iodide, magnesium iodide, calcium iodide; or

a phase transfer catalyst.

4. The process as claimed in claim 1 , wherein said organic base is selected from the group consisting of pyridine, triethylamine, N,N-diethylaniline, and N, N-dimethylaniline.

5. A process for producing γ-mangostin as claimed in claim 1 , comprising the steps of:

Step 1: preparation of pure O-methyl xanthone, semi pure O-methyl xanthone or mixtures of O-methyl xanthones of the general formula I, from a plant source selected from the group consisting of Garcinia mangostana, Garcinia cowa, Garcinia dulcis, Garcinia fusca, Garcinia speciosa, Hydnocarpus species, Cratoxylum formosurn, Allanblackia monticola, Cratoxylurn cochinchinense , and mixtures thereof;

Step 2: dissolving said pure O-methyl xanthone, said semi pure O-methyl xanthone or said mixtures of O-methyl xanthones of the general formula I in an organic solvent to produce a solution;

Step 3: treating the solution with an organic base and stabilizing the solution for a suitable period of time;

Step 4: subsequent to step (3), treating the solution with a Lewis acid and optionally with a catalyst at room temperature to produce a reaction mixture, followed by refluxing the reaction mixture for a suitable period of time, until said pure O-methyl xanthone, said semi pure O-methyl xanthone or said mixtures of O-methyl xanthones are converted to γ-mangostin;

Step 5: quenching the reaction by pouring the reaction mixture into a mixture of ice water, an acid, and brine;

Step 6: extracting the said acidified reaction mixture with an organic solvent; and

Step 7: adding an organic base, to the organic layer prior to evaporating the solvent under vacuum to yield γ-mangostin.

6. The process as claimed in claim 5 , wherein said Lewis acid in step 4 is selected from the group consisting of aluminum chloride, aluminum bromide, aluminum iodide, boron tribromide, boron trichloride-methyl sulfide complex, boron trichloride, boron trifluoride, zinc chloride or iron chloride.

7. The process as claimed in claim 5 , wherein the catalyst is a metal iodide selected from the group consisting of sodium iodide, potassium iodide, magnesium iodide, calcium iodide or a phase transfer catalyst like tetrabutylammonium bromide.

8. The process as claimed in claim 5 , wherein said organic solvent used in step 2 is selected from the group consisting of dichloromethane, dichloroethane, or ethyl acetate.

9. The process as claimed in claim 5 , wherein said organic base used in step 3 is selected from the group consisting of pyridine, triethylamine, N,N-diethylaniline, and N,N-dimethylaniline.

10. The process as claimed in claim 5 , wherein said organic base used in step 7 is selected from the group consisting of pyridine, triethylamine, N,N-diethylaniline, and N,N-dimethylaniline.

11. The process as claimed in claim 5 , further comprising purifying γ-mangostin by subjecting the γ-mangostin to column chromatography on a solid support;

wherein the solid support for column chromatography is selected from the group consisting of silica gel, reversed phase silica gel, styrene-divinylbenzene resin, R20 resin or anion exchange resin.

12. A process for producing γ-mangostin as claimed in claim 1 , wherein:

a) said at least one O-methyl xanthone is a mixture comprising 10-40% by wt. of α-mangostin, 0.5-2% by wt. of β-mangostin and 0.1-0.5% by wt. of γ-mangostin;

b) said step (i) comprises demethylating said at least one O-methyl xanthone to produce a product containing 10-40% by wt. of γ-mangostin; and

c) said step (ii) comprises purifying said product by at least one of chromatography and crystallization to produce γ-mangostin having a purity of 90-99% by wt.

13. A process for producing γ-mangostin as in claim 1 , wherein:

a) said at least one O-methyl xanthone comprise 40-70% by wt. of α-mangostin;

b) said step (i) comprises demethylating said at least one O-methyl xanthone to produce a product containing 40-70% by wt. of γ-mangostin; and

c) said step (ii) comprises purifying said product by at least one of chromatography and crystallization to produce γ-mangostin having a purity of 90-99% by wt.

14. A process for producing γ-mangostin as in claim 1 , wherein:

a) said at least one O-methyl xanthone comprise 70-95% by wt. of α-mangostin;

b) said step (i) comprises demethylating said at least one O-methyl xanthone to produce a product containing 70-95% by wt. of γ-mangostin; and

c) said step (ii) comprises purifying said product by at least one of chromatography and crystallization to produce γ-mangostin having a purity of 90-99% by wt.

15. A process for producing γ-mangostin as in claim 1 , wherein:

a) said at least one O-methyl xanthone comprise 95-99% by wt. of α-mangostin;

b) said step (i) comprises demethylating said at least one O-methyl xanthone to produce a product containing 95-99% by wt. of γ-mangostin; and

c) said step (ii) comprises purifying said product by at least one of chromatography and crystallization to produce γ-mangostin having a purity of 99% by wt.

16. A process for producing γ-mangostin as in claim 1 , wherein:

a) said at least one O-methyl xanthone comprise 99% by wt. of α-mangostin;

b) said step (i) comprises demethylating said at least one O-methyl xanthone to produce a product containing more than 99% by wt. of γ-mangostin.

17. A process for producing γ-mangostin, from at least one O-methyl xanthone other than α-mangostin, wherein said at least one O-methyl xanthone is first converted to α-mangostin by a first demethylating reagent and the α-mangostin so obtained is then demethylated using a second demethylating agent comprising an organic base and a Lewis acid to obtain γ-mangostin.

18. A process as claimed in claim 17 , wherein the first demethylating reagent for producing α-mangostin is sodium cyanide in dimethylsulfoxide.

19. A process for producing γ-mangostin from at least one O-methylxanthone of general formula I, wherein each of R 1 , R 2 , R 3 , and R 4 is either H or CH 3 , wherein a) at least one of R 1 , R 2 , R 3 , and R 4 is CH 3 , and b) said at least one O-methylxanthone is not α-mangostin;

said method comprising:

demethylating said at least one O-methylxanthone with a first demethylating agent to produce α-mangostin; and

demethylating said α-mangostin with a second demethylating agent to produce γ-mangostin, said second demethylating agent comprising an organic base and a Lewis acid.

20. A process for producing γ-mangostin as claimed in claim 19 , wherein said at least one O-methyl xanthone comprises a compound selected from the group consisting of; 1,6-dihydroxy-3,7-dimethoxy-2,8-bis-(3-methyl-but-2-enyl)-xanthen-9-one (β-mangostin, R 1 ═R 3 ═H, R 2 ═R 4 ═CH 3 ); 1,3-dihydroxy-6,7-dimethoxy-2,8-bis-(3-methyl-but-2-enyl)-xanthen-9-one (R 1 ═R 2 ═H, R 3 ═R 4 ═CH 3 ); 1-hydroxy-3,6,7-trimethoxy-2,8-bis-(3-methyl-but-2-enyl)-xanthen-9-one (R 1 ═H, R 2 ═R 3 ═R 4 ═CH 3 ); and mixtures thereof.

21. A process for producing γ-mangostin as claimed in claim 19 , wherein said at least one O-methyl xanthone is derived from a plant selected from Garcinia mangostana, Garcinia cowa, Garcinia dulcis, Garcinia fusca, Garcinia speciosa, Hydnocarpus species, Cratoxylum formosum, Allanblackia monticola, Cratoxylum cochinchinense.

22. A process for producing γ-mangostin as claimed in claim 19 wherein said at least one O-methyl xanthone, is of semisynthetic origin obtained from xanthones isolated from a plant selected from Garcinia mangostana, Garcinia cowa, Garcinia dulcin, Garcinia fusca, Garcinia speciosa, Hydnocarpus species, Cratoxylum formosum, Allanblackia monticola, Cratoxylum cochinchinense.

23. A process for producing γ-mangostin as claimed in claim 19 , wherein said at least one O-methyl xanthone is a pure compound or a partially pure compound obtained as a plant extract or an enriched plant extract or a mixture having the chemical structure(s) corresponding to the general formula I.

24. A process for producing γ-mangostin as claimed in claim 19 , wherein the concentration of said at least one O-methyl xanthone in the starting mixture is in the range of 5% to 99%.

25. A process for producing γ-mangostin as in claim 23 , wherein the concentration of said at least one O-methyl xanthone in the starting mixture is in the range of 5% to 99%.

Assignments (3)
CHANGE OF NAME Recorded Aug 18, 2025
From: LAILA NUTRACEUTICALS
To: LAILA NUTRA PRIVATE LIMITED
Reel/Frame 072508/0229 →
CORRECTIVE ASSIGNMENT TO CORRECT THE SPELLING OF ASSIGNOR, SOMEPALLI, VENKATEWARLU PREVIOUSLY RECORDED ON REEL 024705 FRAME 0837. ASSIGNOR(S) HEREBY CONFIRMS THE NAME OF ASSIGNOR, SOMEPALLI, VENKATESWARLU. Recorded Aug 12, 2010
From: GOKARAJU, GANGA RAJU; GOKARAJU, RAMA RAJU; GOLAKOTI, TRIMURTULU; SOMEPALLI, VENKATESWARLU; BHUPATHIRAJU, KIRAN
To: LAILA NUTRACEUTICALS
Reel/Frame 024829/0093 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 19, 2010
From: GOKARAJU, GANGA RAJU; GOKARAJU, RAMA RAJU; GOLAKOTI, TRIMURTULU; SOMEPALLI, VENKATEWARLU; BHUPATHIRAJU, KIRAN
To: LAILA NUTRACEUTICALS
Reel/Frame 024705/0837 →
Priority Claims (1)
WO PCT/IN2008/000040 · Jan 21, 2008 · international
Continuity (1)
Related Publication 20100292490A1 · Nov 18, 2010